CONTROLLING THERMAL ENERGY STORAGE

20220187028 · 2022-06-16

Assignee

Inventors

Cpc classification

International classification

Abstract

A method of flattening electric energy demand from an electric grid including during less-than-peak electricity demand periods, freezing Phase Change Material (PCM) in a Thermal Energy Storage (TES) system, and during peak electricity demand periods, using the TES to cool air conditioning refrigerant fluid. A system of flattening electric energy demand of an air-conditioner from an electric grid including an air conditioner, a Thermal Energy Storage system, and a controller, wherein the controller is programmed to implement the above method. A method of freezing Phase Change Material (PCM) in a Thermal Energy Storage (TES) system including setting a temperature of heat exchange fluid at a temperature higher than −10 degrees Celsius when directed to ice bricks containing water and an ice nucleation agent. A Thermal Energy Storage (TES) system controller programmed to discharge more than 50% of a heat capacity of the TES. Related apparatus and methods are also described.

Claims

1-26. (canceled)

27. A method for enabling an electric client facility to control electric consumption at a facility, the method comprising: an electric client facility: using an air conditioner cooling system to cool a refrigerant flow of the air conditioner; using a controller to monitor cost of electricity from a power company; and, based on the monitoring, when cost of electricity rises, then using the controller to switch to using a Thermal Energy Storage (TES) system to cool the refrigerant flow of the air conditioner, thereby lowering electric consumption, else continuing to use the chiller of the air conditioner. thereby enabling the electric client facility to control electric consumption at the facility.

28. A method according to claim 27, wherein monitoring cost of electricity from a power company comprises monitoring a client facility meter.

29. A method according to claim 27, wherein using the TES system to cool the refrigerant of the air conditioner is performed based on when electrical demand approaches a contractual obligation of the client.

30. A method according to claim 27, comprising predicting when peak electric demand charges are anticipated; and using a TES system to cool the refrigerant of the air conditioner when peak electric demand charges are anticipated,

31. A method of freezing Phase Change Material (PCM) in a Thermal Energy Storage (TES) system comprising setting a temperature of heat exchange fluid at a temperature higher than −5 degrees Celsius when directed to ice bricks containing water.

32. A method according to claim 27, used for mitigating electricity costs caused by charging an electric vehicle.

33. A method according to claim 31, wherein charging of the electric vehicle is stopped when cost of electricity rises.

34. A method according to claim 31, comprising taking electricity charged in the electric vehicle for use at the facility when cost of electricity rises.

35. A method according to claim 27, used for preventing reaching an upper limit of electric consumption at a facility.

36. A method according to claim 27, used for mitigating CO.sub.2 emissions caused by electric consumption comprising: monitoring CO.sub.2 emissions corresponding to use of electricity at a facility; and using a TES system to cool the refrigerant of the air conditioner at high-CO.sub.2 emission periods, thereby lowering CO.sub.2 emissions.

37. A method according to claim 27, used for controlling an interrupted mode of operation of an air conditioning system, comprising: detecting when an air conditioner turns on or turns off; estimating churn based on the detecting; when churn estimate indicates a compressor of the air conditioner is churning, then using the TES system to cool the refrigerant of the air conditioner, else continuing to use the compressor of the air conditioner.

38. A method according to claim 27, comprising: monitoring phase angle between conductors in a three phase electric system providing electricity to the air conditioner; when phase angle is different from a nominal phase angle by more than a threshold value, then using a TES system to cool the refrigerant of the air conditioner, else continuing to use the air conditioner cooling system of the air conditioner.

39. A method according to claim 27, comprising: monitoring phase imbalance between conductors in a three phase electric system providing electricity to the air conditioner; when phase imbalance is greater than a threshold value, then using a TES system to cool the refrigerant of the air conditioner, else continuing to use the air conditioner cooling system of the air conditioner.

40. A method according to claim 27, used for mitigating electricity costs caused by imbalance in a three phase electric circuit, comprising: monitoring cost of electricity from power company; and when cost of electricity rises due to phase drift, then using a TES system to cool refrigerant of the air conditioner, else continuing to use the air conditioner cooling system of the air conditioner.

41. A method according to claim 27, comprising: receiving a control signal; and instructing a fluid distribution system to direct heat exchange fluid of an air-conditioner from flowing through a condensing coil to flowing through the TES system.

42. A method according to claim 27, comprising: during less-than-peak electricity demand periods, freezing Phase Change Material (PCM) in the TES system; and during peak electricity demand periods, using the TES to cool air conditioning refrigerant fluid.

43. A method according to claim 27, used by an establishment selected from a group consisting of: a server farm; a residential building; a shopping center; an office building; a hotel; a hospital; a small scale energy center; a medium scale energy center; a large scale energy center; a small scale cooling system; a medium scale cooling system; and a large scale cooling system.

44. A client system for controlling electricity costs, the system comprising: an air conditioner; a Thermal Energy Storage system; and a controller, wherein the controller is programmed to implement the method of claim 27.

45. The system of claim 44, capable of discharging more than 80% of a heat capacity of the TES.

46. The system of claim 44, wherein the system is configured to control flow of refrigerant fluid from the air conditioner through the TES.

Description

BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWING(S)

[0145] The invention is herein described, by way of example only, with reference to the accompanying drawings. With specific reference now to the drawings in detail, it is stressed that the particulars shown are by way of example and for purposes of illustrative discussion of the preferred embodiments of the present invention only, and are presented in order to provide what is believed to be the most useful and readily understood description of the principles and conceptual aspects of the invention. In this regard, no attempt is made to show structural details of the invention in more detail than is necessary for a fundamental understanding of the invention, the description taken with the drawings making apparent to those skilled in the art how the several forms of the invention may be embodied in practice.

[0146] Some embodiments of the invention are herein described, by way of example only, with reference to the accompanying drawings. With specific reference now to the drawings in detail, it is stressed that the particulars shown are by way of example and for purposes of illustrative discussion of embodiments of the invention. In this regard, the description taken with the drawings makes apparent to those skilled in the art how embodiments of the invention may be practiced.

[0147] In the drawings:

[0148] FIGS. 1A-1E are schematic diagrams of a thermal energy storage system according to at least some embodiments of the present invention;

[0149] FIGS. 2A-2Y are illustrations of ice bricks, ice capsules and thermal storage arrays according to at least some embodiments of the present invention;

[0150] FIG. 3 shows an ice capsule according to at least some embodiments of the present invention;

[0151] FIG. 4 shows a cylindrical ice brick according to at least some embodiments of the present invention;

[0152] FIG. 5A shows a TES system capable of activating separate subsets of ice bricks by a controller.

[0153] FIG. 5B shows a flow diagram for operation of a TES system.

[0154] FIG. 5C shows experimental data from operation of a TES system according to at least some embodiments of the present invention;

[0155] FIGS. 6A-6G show spacers for use in an ice brick according to at least some embodiments of the present invention;

[0156] FIGS. 7A to 7D show a thermal energy storage unit and cross-sectional views of a thermal energy storage unit including the tube and capsules according to at least some embodiments of the present invention;

[0157] FIGS. 8A and 8B show capsules containing metal strips according to at least some embodiments of the present invention;

[0158] FIGS. 9A and 9B show spacers between capsules according to at least some embodiments of the present invention;

[0159] FIG. 10A is a simplified flow chart illustration of a method for controlling use of higher heat discharge rate bricks and lower heat discharge rate bricks according to an example embodiment of the invention;

[0160] FIG. 10B is a simplified flow chart illustration of a method for controlling use of higher heat discharge rate bricks and lower heat discharge rate bricks according to an example embodiment of the invention;

[0161] FIG. 10C is a simplified flow chart illustration of a method for controlling rate of freezing or cooling heat transfer fluid according to an example embodiment of the invention;

[0162] FIG. 11A is a simplified flow chart illustration of a method for flattening electric energy demand from an electric grid according to an example embodiment of the invention;

[0163] FIG. 11B is a simplified block diagram illustration of a system for flattening electric energy demand from an electric grid according to an example embodiment of the invention;

[0164] FIG. 12A is a simplified flow chart illustration of a method for controlling an interrupted mode of operation of a compressor in an air conditioning system according to an example embodiment of the invention;

[0165] FIG. 12B is a simplified flow chart illustration of a method for mitigating imbalance in a three phase electric circuit according to an example embodiment of the invention; and

[0166] FIG. 12C is a simplified flow chart illustration of a method for mitigating electricity costs caused by imbalance in a three phase electric circuit according to an example embodiment of the invention;

[0167] FIG. 12D is a simplified flow chart illustration of a method for mitigating electricity costs caused by charging electric vehicles at a facility according to an example embodiment of the invention;

[0168] FIG. 12E is a simplified flow chart illustration of a method for mitigating electricity costs caused by peak electric demand charges according to an example embodiment of the invention;

[0169] FIG. 12F is a simplified flow chart illustration of a method for mitigating CO.sub.2 emissions caused by electric consumption according to an example embodiment of the invention;

[0170] FIG. 12G is a simplified flow chart illustration of a method for preventing reaching an upper limit of electric consumption at a facility according to an example embodiment of the invention; and

[0171] FIG. 12H is a simplified flow chart illustration of a method for mitigating frequency drift in an electric circuit according to an example embodiment of the invention.

DESCRIPTION OF SOME SPECIFIC EMBODIMENTS OF THE INVENTION

[0172] The present invention, in some embodiments thereof, relates to a system and method for thermal energy storage and particularly but not exclusively to controlling use of and applications for thermal energy storage, and even more particularly but not exclusively to software and components for controlling efficiency of thermal energy storage.

[0173] The controlling use of and applications for thermal energy storage, and the software and components for controlling efficiency of thermal energy storage are applicable to various types of systems for thermal energy storage, including Thermal Energy Systems (TES) systems as described in above-mentioned International Patent Application Number PCT/IB2018/001091, various “ice-on-coil” storage systems, “encapsulated ice” systems, and other TES systems.

[0174] Methods and devices for controlling use of and applications for thermal energy storage are described herein in addition to descriptions taken from International Patent Application Number PCT/IB2018/001091 for thermal energy storage systems which are suitable for being used with the above-mentioned methods, devices and applications.

[0175] The present application describes how to implement some methods, devices and applications for other, additional thermal energy storage systems such as ice-on-coil systems, and even energy storage systems such as battery storage.

[0176] Before explaining at least one embodiment of the invention in detail, it is to be understood that the invention is not necessarily limited in its application to the details of construction and the arrangement of the components and/or methods set forth in the following description and/or illustrated in the drawings and/or the Examples. The invention is capable of other embodiments or of being practiced or carried out in various ways.

[0177] Various exemplary control methods of Thermal Energy Storage (TES) systems will be described below, which apply to: (a) TES systems as described herein with reference to FIGS. 1A-9B; (b) TES systems which include a mix of TES systems as described herein with reference to FIGS. 1A-9B and TES systems which do not share inventive aspects with the TES systems as described herein with reference to FIGS. 1A-9B; and (c) TES systems which do not share inventive aspects with the TES systems as described herein with reference to FIGS. 1A-9B.

[0178] Where TES systems are mentioned herein, additional systems can also be used, or combined, and in some cases a tradeoff between systems is optionally made based on cost, capacity, etc.

[0179] TES systems as described herein with reference to FIGS. 1A-9B can potentially provide a high rate of discharge, potentially maintain the high rate of discharge stable over a relatively long period of time, and potentially achieve a high percentage of depth of discharge, relative to similarly sized other systems.

[0180] In some embodiments, TES systems as described herein, by using multiple capsules, and/or by providing a high heat transfer area to stored volume ratio, and/or by maintaining turbulent flow patterns, can potentially achieve the high rate of discharge even when 80% or more of the stored energy is already consumed.

[0181] For example, in some embodiments, TES systems as described herein can potentially discharge up to ˜90-92% of the stored energy within a 4 hour period.

[0182] Controlling Systems Having Mixed Higher Heat Discharge Rate and Lower Heat Discharge Rates

[0183] In some embodiments, some ice bricks or TES units in a TES system are ice bricks have a relatively higher heat discharge rate and some ice bricks have a relatively lower heat discharge rate.

[0184] Some example values:

[0185] The term low rate of heat discharge is used herein to mean less than 90% discharge depth during 6 or more hours of discharge.

[0186] The term medium rate of heat discharge is used herein to mean more than 90% discharge depth during 4 hours of discharge.

[0187] The term high rate of heat discharge is used herein to mean more than 85% discharge depth during 2 hours of discharge.

[0188] The term very-high rate of heat discharge is used herein to mean more than 75% discharge depth during 1 hours of discharge.

[0189] In various embodiments, TES systems as described herein achieve all of the above-mentioned low, medium, high and very-high rates of heat discharge.

[0190] In some embodiments, a mix of higher heat discharge rate bricks and lower heat discharge rate bricks potentially enable producing TES systems with improved capabilities over previous such systems.

[0191] In some embodiments, a controller is optionally used to control when and how much energy is drawn from the higher heat discharge rate bricks and when and how much energy is drawn from the relatively lower heat discharge rate bricks.

[0192] It is noted that combining higher heat discharge rate bricks and lower heat discharge rate bricks potentially enables providing an immediate cooling effect, optionally followed by a long term continuing cooling effect.

[0193] It is noted that if higher heat discharge rate bricks are more expensive than lower heat discharge rate bricks, combining the two types potentially enables providing a lower-total-cost system which can potentially provide both immediate cooling and longer term cooling.

[0194] In some embodiments, installation space may forces or allows to use a specific mix.

[0195] It is noted that if higher heat discharge rate bricks are more (or less) efficient in volume/space consumption than lower heat discharge rate bricks, combining the two types potentially enables providing a lower-total-cost system which can potentially answer a specific volume/space consumption while potentially keeping system costs down.

[0196] Some configurations which potentially produce higher-heat-discharge-rate ice bricks include:

[0197] Increasing a heat transfer area to stored heat ratio by making the capsules narrower.

[0198] Making the capsules of superior heat transfer material such as metal and/or Heat Transfer Plastic.

[0199] Including turbulence inducers between the capsules, optionally adjustable turbulence inducers.

[0200] Including heat transfer fins in the capsules.

[0201] In some embodiments several groups of containers with different discharge characteristics potentially provide heat capacity for at least two heat demand regimes—by way of a non-limiting example a first regime providing X refrigeration tons (RTH) suitable for a regime of load shift (for example for 4 hours) and providing Y refrigeration tons (RTH) suitable for grid demand or other high discharge requirements, for example 1 to 2 hours of high discharge rate, and optionally 10-15 minutes of Z refrigeration tons during specific hours and/or as a response to a request, optionally from a power grid manager.

[0202] In some embodiments several groups of containers with different discharge characteristics are optionally used at a same time.

[0203] In some embodiments, a controller is optionally used to control when and how much energy is stored into the higher heat discharge rate bricks and when and how much energy is stored into the relatively lower heat discharge rate bricks.

[0204] In some embodiments, a controller, or a control program, optionally uses a greedy algorithm which matches which ice brick to charge based on a capacity, rate, fill level, expected size of charge, etc. of the ice brick.

[0205] In some embodiments, a controller, or a control program, optionally uses an economic optimization algorithm which matches which ice brick to charge based on a capacity, rate, fill level, expected size of charge, etc. of the ice brick.

[0206] In some embodiments, the control program includes data such as an efficiency curve and/or a rate curve per ice brick type of even per specific ice brick, and the control program uses the data to make decisions (while taking into account predictions of when the stored energy will be needed, and optionally actual cost of electricity and energetic cost to make/use ice).

[0207] Reference is now made to FIG. 10A, which is a simplified flow chart illustration of a method for controlling use of higher heat discharge rate bricks and lower heat discharge rate bricks according to an example embodiment of the invention.

[0208] In some embodiments a combination of higher heat discharge rate bricks and lower heat discharge rate bricks is controlled as shown in FIG. 10A:

[0209] a controller determines what heat discharge schedule is desired (1002);

[0210] at a beginning of the schedule a first rate of heat discharge rate bricks are optionally used (1004); and

[0211] later on in the schedule a second rate of heat discharge rate bricks are optionally used (1006).

[0212] In some embodiments, the controller determines what heat discharge schedule is desired based on recording a historic heat discharge schedule for previous days, for a weekly cycle, and so on.

[0213] In some embodiments, a control program is fed with a desired heat discharge schedule.

[0214] In some embodiments, the controller determines what heat discharge schedule is desired based on taking into account a weather forecast.

[0215] In some embodiments, the controller determines what heat discharge schedule is desired based on taking into account known variances in a length of sunshine over a yearly schedule.

[0216] Reference is now made to FIG. 10B, which is a simplified flow chart illustration of a method for controlling use of higher heat discharge rate bricks and lower heat discharge rate bricks according to an example embodiment of the invention.

[0217] In some embodiments a combination of higher heat discharge rate bricks and lower heat discharge rate bricks is controlled as shown in FIG. 10B:

[0218] A controller determines what heat discharge rate is desired (1012);

[0219] If a requirement is for a higher heat discharge rate, higher heat discharge rate bricks are optionally used (1014); and

[0220] If a requirement is for a lower heat discharge rate, lower heat discharge rate bricks are optionally used (1016).

[0221] In some embodiments the controller provides a heat discharge rate based on a schedule stored in the controller. In some embodiments the controller provides a heat discharge rate based on a schedule received by the controller, by way of a non-limiting example received by electronic means, wired or wireless, by way of a non-limiting example received from a power supply company, from an air-conditioning client, and so on.

[0222] In some embodiments the controller compares a desired schedule with predicted capacity, and controls storing energy to provide for the capacity.

[0223] In some embodiments the controller compares a desired schedule with predicted capacity, and optionally communicates a warning that capacity is not up to the predicted load, potentially hours or even days (based on weather forecast for example) before the predicted lack of capacity.

[0224] In some embodiments, during an early period of operation, fully charged bricks, both high discharge rate bricks and low discharge rate bricks, can support a high discharge rate, since most of the capsules are frozen. The high heat discharge rate capsules are optionally “saved” in a standby mode until a last portion of the discharge period, thus allowing fast response even if a big portion of the total installed heat capacity has been used.

[0225] In some embodiments a controller or control software optionally takes into account a contractual status of heat provision of an installation in deciding which mode to use first high heat-discharge-rate or low heat-discharge-rate. By way of a non-limiting example, once the heat provision system fails, for example once in a month, to support a specific fast demand requirement, the heat provision system or company is penalized just this once a month and the control software optionally decides to use stored energy for load shifting only.

[0226] In some embodiments the controller of control software is optionally updated with monthly, weekly, daily, hourly, or even minute-by-minute contractual obligations and in some cases, optionally, the commercial value of the contractual obligations.

[0227] In some embodiments a client facility meter is optionally used as an input to support control decisions regarding peak demand energy saving.

[0228] In some embodiments instead of a simple pre-determined load shifting profile control software is optionally used to inject cooling capacity and/or reduce chillers power consumption when the client facility electrical demand approaches a contractual obligation of the client. In some embodiments, an energy demand above the contractual obligation may be followed by high demand charges. In some cases the commercial value of the high demand charges is higher than the commercial value of shifted kWhrs (KiloWatt-Hours).

[0229] In some embodiments control software optionally monitors an operating point of facility chiller(s) which supply cooling requirements of a facility. Based on predefined data related to Best Efficiency Point(s) [BEP] of the chillers and the commercial value of electricity during a specific period, a controller optionally instructs the energy or heat storage system to increase or decrease cooling capacity injected into a cooling consumer, in order to potentially shift a chiller's operating point to the BEP of the chiller.

[0230] In some embodiments control software optionally monitors a temperature of heat transfer fluid required by facility chiller(s) which supply cooling requirements of a facility. Based on the required temperature, a controller optionally instructs the energy or heat storage system to increase or decrease heat transfer fluid temperature injected into a cooling consumer.

[0231] Some non-limiting examples of measured values or status values are: chiller(s)′ electrical load; chiller(s)′ cooling load; client facility actual load; ambient temperature; and remaining cooling capacity in the TES.

[0232] In some embodiments, a difference between each chiller's actual operation point and power consumption (in kW) and a related efficiency (data available from a chiller's supplier) is optionally calculated. The calculation results are optionally compared to an expected efficiency and power consumption which can be achieved if the load on the chiller is changed to BEP by increasing or decreasing the load using TES energy, such calculation optionally based on Chiller supplier data, the controller potentially identifies economic gain, and optionally switches to use TES energy.

[0233] A TES System with High Discharge Capability

[0234] In some embodiments, for example such as described herein and such as described in above-mentioned International Patent Application Number PCT/IB2018/001091, a TES system can potentially discharge a high percentage of the heat stored therein.

[0235] In some embodiments, a Thermal Energy Storage (TES) system is provided which is capable of discharging more than, for example, 50-70% of a heat capacity of the TES during 1 hour, or 80% during 2 hours. In some embodiments, a Thermal Energy Storage (TES) system is provided which is capable of discharging more than 92% of a heat capacity of the TES during 4 hours of discharge. In some embodiments, a Thermal Energy Storage (TES) system is provided which is capable of discharging any desired percentage value in a range between 0% and 100% of a heat capacity of the TES, optionally at a desired discharge rate. The controller potentially uses one or more inputs such as desired percentage of discharge, desired rate of discharge, desired duration of discharge, to determine at what temperature to provide and/or at what flow rate to provide HTF.

[0236] In some embodiments, a Thermal Energy Storage (TES) system is provided which includes a controller set to discharge more than 50% of a heat capacity of the TES. In some embodiments, the controller is set to discharge more than 80% of a heat capacity of the TES. In some embodiments, the controller is set to discharge a percentage value in a range between 0% and 80% of a heat capacity of the TES. In some embodiments, the controller is set to discharge a percentage value in a range between 60% and 95% of a heat capacity of the TES.

[0237] The controller or a control program optionally includes storage memory for storing parameter such as required discharge percentage, required discharge rate, and so on.

[0238] Controlling Rate of Freezing or Cooling Heat Transfer Fluid

[0239] In some embodiments one or more sensors are optionally used to sense a state of an ice brick or a thermal storage array—a state such as whether the ice brick has started to freeze; is completely frozen; has reached a specific temperature difference between incoming fluid and outgoing fluid.

[0240] In some embodiments the sensor is an ultrasound sensor, potentially sensing a difference between frozen matter and liquid matter.

[0241] In some embodiments the sensor measures impedance or resistivity, potentially sensing a difference between frozen matter and liquid matter.

[0242] In some embodiments sensors measure temperature of various locations of an ice brick, e.g. fluid entrance and/or exit into ice brick and/or within the ice brick.

[0243] In some embodiments the sensor is built into an ice brick array. In some embodiments the sensor is built into an ice brick.

[0244] In some embodiments sensor(s) measurement(s) is/are optionally used to control a rate of freezing ice bricks or using the ice bricks for cooling, by controlling various control parameters applicable to freezing the ice bricks or using the ice bricks for cooling. Such control parameters potentially include, by way of some non-limiting examples, temperature of heat transfer fluid, rate of flow of heat transfer fluid, pressure of heat transfer fluid.

[0245] In some embodiments heat transfer fluid is controlled to be provided at a lower temperature, for example in a range between −12 and −8 degrees Celsius, to reach a beginning of freezing of an ice brick, and subsequently controls heat transfer fluid to be provided at a relatively higher temperature, optionally at higher temperature as enabled by the more efficient ice bricks described herein, for example in a range of temperature between −8 degrees Celsius and −2.7 degrees Celsius.

[0246] In some embodiments heat transfer fluid is controlled to be provided at a higher flow rate to reach a beginning of freezing of an ice brick, and subsequently controlled to be provided at a relatively lower flow rate, as enabled by the more efficient ice bricks described herein.

[0247] In some embodiments, by way of a non-limiting example, a TES system as described herein is requested to provide a nominal 0.6 m.sup.3 per hour per Refrigeration Ton. In some embodiments, the flow rate of the HTF may be may be 0.6 m.sup.3 per hour at the nominal temperature. In some embodiments, the flow rate of the HTF may be may be proportionally higher than 0.6 m.sup.3 per hour, at a higher-than-nominal temperature or load demand. In some embodiments, the flow rate of the HTF may be proportionally lower than 0.6 m.sup.3 per hour, at a lower-than-nominal temperature or load demand.

[0248] Reference is now made to FIG. 10C, which is a simplified flow chart illustration of a method for controlling rate of freezing or cooling heat transfer fluid according to an example embodiment of the invention.

[0249] The method of FIG. 10C includes:

[0250] cooling an ice brick at with heat transfer fluid at a first cooling temperature (1022);

[0251] receiving sensor measurements from the ice brick (1024);

[0252] estimating the state of the ice brick (1026); and

[0253] if the ice brick is estimated to be frozen, then cooling the ice brick with heat transfer fluid at a second, higher cooling temperature (1028),

[0254] else continuing to cool the ice brick with heat transfer fluid at the first cooling temperature (1029).

[0255] Flattening Electric Energy Demand

[0256] In some embodiments energy provided during less-than-peak electricity demand periods is optionally used to freeze Phase Change Material (PCM) in a Thermal Energy Storage (TES) system, and optionally used to cool air conditioning refrigerant fluid during peak electricity demand periods.

[0257] Reference is now made to FIG. 11A, which is a simplified flow chart illustration of a method for flattening electric energy demand from an electric grid according to an example embodiment of the invention.

[0258] The method of FIG. 11A includes:

[0259] during less-than-peak electricity demand periods, freezing Phase Change Material (PCM) in a Thermal Energy Storage (TES) system (1102);

[0260] during peak electricity demand periods, using the TES to cool air conditioning refrigerant fluid (1104).

[0261] In some embodiments the above method is optionally used by a server farm, a residential building, shopping centers, offices, hotels, hospitals, and additional commercial small, medium and large scale energy centers and/or cooling systems

[0262] In some embodiments the TES system includes a radio receiver, and optionally receives a radio signal from an electric power supply company transmitter indicating a peak electricity demand period.

[0263] In some embodiments the TES system includes an Internet connection, and optionally receives an internet message from the electric power supply company transmitter indicating a peak electricity demand period.

[0264] In some embodiments the TES system is configured as an Internet-of-Things device, and optionally receives an instruction from the electric power supply company transmitter indicating a peak electricity demand period.

[0265] Reference is now made to FIG. 11B, which is a simplified block diagram illustration of a system for flattening electric energy demand from an electric grid according to an example embodiment of the invention.

[0266] FIG. 11B shows a power company 1122, and a system 1120 which includes an air conditioner 1124, a TES unit or system 1128 and a controller 1126.

[0267] Various example embodiments of the system are described below, of potential scenarios of using the system 1120 in a manner which flattens electric energy demand from an electric grid.

[0268] The power company 1122 provides electric power 1121 to the air conditioner 1124.

[0269] In some embodiments, by way of a non-limiting example during peak electric power demand, the power company 1122 optionally sends a message 1123 to the controller 1126.

[0270] The message 1123 may be an instruction to enter an electric-power saving mode, as described below. In some embodiments, the message 1123 may be a schedule for when the system 1120 should enter the electric-power saving mode.

[0271] In some embodiments, the controller 1126 controls the system 1120 to enter (or leave) electric-power saving mode.

[0272] To enter electric-power saving mode, the controller 1126 may instruct 1125 1127 the TES system 1128 and the air conditioner 1124 to use cooling fluid 1129 from the TES system 1128 rather than use the air conditioner's compressor, thereby lowering energy demand by the air conditioner 1124.

[0273] To leave electric-power saving mode, the controller 1126 may instruct 1125 1127 the TES system 1128 and the air conditioner 1124 to stop using cooling fluid 1129 from the TES system 1128, and use the air conditioner's compressor.

[0274] In some embodiments the power company 1122 is potentially connected to several/many such systems 1120, and optionally flattens or lowers total electricity demand by instructing some systems 1120 to use their TES 1128 for cooling and some to use electricity 1121, optionally rotating electric-energy-saving mode among the different systems 1120.

[0275] In some embodiments, the signal 1123 is optionally a radio signal, as is used in some localities by power companies to stop air-conditioners equipped with compatible receivers.

[0276] In some embodiments, the signal 1123 is optionally conveyed over the Internet.

[0277] In some embodiments, the controller 1126 and/or the air conditioner 1124 and/or the TES 1128 and/or system 1120 use the Internet of Things protocol for communicating or receiving instructions from the power company 1122.

[0278] In some embodiments, such as described in FIGS. 11A and 11B above, an air conditioner optionally turns its compressor OFF and/or ON based on a power company sending a message or a schedule.

[0279] In some embodiments, such as described in FIGS. 11A and 11B above, an air conditioner 1124 or a TES system 1128 or a controller 1126 optionally controls a flow path of cooling fluid 1129, so that the cooling fluid 1129 is cooled either by flowing through a compressor or by flowing through the TES system 1128.

[0280] In some embodiments, potentially based on grid electricity demand and/or a signal from an electric power supply company, the system 1120 optionally turn off a compressor of the air conditioner 1124 even for short periods, such as 2, 3, 5, 10 minutes, and use the TES system 1128 for cooling instead.

[0281] In some embodiments such short periods are potentially made possible based on a rapid response to cooling by high-heat-discharge rate ice bricks as described herein.

[0282] It is noted that such a load balancing can potentially occur within seconds, and potentially last for a period of seconds, minutes and even hours.

[0283] In some embodiments the controller 1126 optionally takes into account a cost of starting and stopping the compressor, in terms of wear-and-tear on the compressor, and compares the compressor wear-and-tear cost to a cost of not switching the compressor off and not taking advantage of cooling stored at lower electricity costs. The controller 1126 is optionally programmed to NOT switch the compressor off if the savings in electricity costs are lower than the cost of wear-and-tear on the compressor.

[0284] Controlling an Interrupted Mode of Operation of a Compressor

[0285] In some cases a compressor of an air conditioner turns on and off frequently, for example when its cooling load is not equal to its cooling power. In some case a compressor of an air conditioner turns on and off frequently, for example when its cooling power quickly overcomes the cooling load, and a thermostat turns the compressor off. Such a frequent turning on and off of a compressor is sometimes called an interrupted mode of operation, or “churn”. In some embodiments, the controller 1126 optionally controls the system 1120 to churn less, by turning the compressor off for longer periods, using the TES 1128 instead.

[0286] Reference is now made to FIG. 12A, which is a simplified flow chart illustration of a method for controlling an interrupted mode of operation of a compressor in an air conditioning system according to an example embodiment of the invention.

[0287] The method of FIG. 12A includes:

[0288] using a compressor in a refrigerant flow of an air conditioner (1201);

[0289] detecting when the air conditioner turns on or turns off (1202);

[0290] estimating churn based on the detecting (1204);

[0291] if churn estimate indicates the compressor is churning (1206), then using a TES system to cool the refrigerant of the air conditioner (1208),

[0292] else continuing to use the compressor of the air conditioner (1210).

[0293] In some embodiments indication of churn is optionally produced by comparing a value of a churn estimate or measure to a churn threshold value.

[0294] In some embodiments indication of churn is optionally produced by using “fuzzy logic” to categorize a value of a churn estimate as likely or not likely to indicate churn.

[0295] It is noted that such a response to detecting churn can potentially occur within seconds, and potentially last for a period of seconds, minutes and even hours.

[0296] In some embodiments a method is provided to control an interrupted mode of operation of a compressor in an air conditioning system and/or some other cooling system, the method including using a compressor in a refrigerant cooling system, detecting when the air conditioner turns on or turns off, estimating churn based on the detecting, when churn estimate indicates the compressor is churning, then using a TES system to cool the refrigerant of the air conditioner, else continuing to use the compressor of the air conditioner.

[0297] Phase Balancing and/or Frequency Stabilization.

[0298] In some cases, an air conditioner works off one phase or one conductor in a three-phase electric supply. However, when the three-phase electric supply is not balanced, by one conductor drawing significantly more electricity than the other two conductors, the phase difference between the three conductors of the three phase electric supply may change. Such an altered phase is called an imbalanced phase.

[0299] In some cases the imbalance causes a change in frequency of the alternating electricity. Such a change of frequency has a potential to undermine circuits or device which depend on the grid frequency.

[0300] Electricity from an imbalanced three phase circuit may provide less power and/or be less efficient, in terms of power and/or cost-to-operate, than electricity from a balanced three phase circuit.

[0301] In some cases, electricity from an imbalanced circuit is more expensive.

[0302] In some cases, when an air conditioning unit, for example such as the air conditioner 1124 of the system 1120 described with reference to FIG. 11B, draws a large load of electricity, the air conditioning unit may cause a phase imbalance.

[0303] A non-limiting example of such imbalance may be caused in a system where an air conditioner compressor receives electricity from one phase conductor of a three phase electrical system, for example a small air conditioning system in a private home.

[0304] In some embodiments a controller optionally monitors the phase difference between phases in three phase electricity supply, and optionally causes the air conditioning unit to switch from using a compressor to using a TES system for cooling the air conditioning refrigerant.

[0305] Reference is now made to FIG. 12B, which is a simplified flow chart illustration of a method for mitigating imbalance in a three phase electric circuit according to an example embodiment of the invention.

[0306] The method of FIG. 12B includes:

[0307] using a compressor in a refrigerant flow of an air conditioner (1222);

[0308] monitoring phase imbalance between conductors in a three phase electric system providing electricity to the air conditioner (1224);

[0309] if phase imbalance is greater than a threshold value (1226), then using a TES system to cool the refrigerant of the air conditioner (1228),

[0310] else continuing to use the compressor of the air conditioner (1230).

[0311] In some embodiments a method is provided to mitigate frequency change, such as frequency drop, when the electricity grid becomes unstable. In some embodiments the method includes monitoring the grid's frequency, and ordering chillers and or compressors used by a Thermal Energy System (TES) to turn off when the electric grid frequency changes, for example drops below a certain threshold. In such a case the electric load potentially drops, by removing the electric load of a compressor of the chillers of the TES. In some embodiments, a signal coming from a grid operator is optionally used to trigger removing the electric load of the compressor of the chillers of the TES. Such services are called ancillaries and are not performed by current ice storage systems due to their slow rate discharge limitations.

[0312] Reference is now made to FIG. 12H, which is a simplified flow chart illustration of a method for mitigating frequency drift in an electric circuit according to an example embodiment of the invention.

[0313] The method of FIG. 12H includes:

[0314] using a compressor in a refrigerant flow of an air conditioner (1292);

[0315] monitoring electric circuit frequency (1293);

[0316] when the frequency declines by more than a threshold value (1294),

[0317] then using a TES system to cool the refrigerant of the air conditioner (1295),

[0318] else (1296) continuing to use the compressor of the air conditioner.

[0319] Mitigating Electricity Costs

[0320] In some cases phase drift causes a power company to increase electricity cost.

[0321] In some embodiments, if price of electricity spikes, for example due to frequency drift or phase imbalance, the controller optionally turn off the compressor, and optionally uses cooling by a TES system.

[0322] Reference is now made to FIG. 12C, which is a simplified flow chart illustration of a method for mitigating electricity costs caused by imbalance in a three phase electric circuit according to an example embodiment of the invention.

[0323] The method of FIG. 12C includes:

[0324] using a compressor in a refrigerant flow of an air conditioner (1242);

[0325] monitoring cost of electricity from power company (1244);

[0326] if cost of electricity rises (1246), then using a TES system to cool the refrigerant of the air conditioner (1248),

[0327] else continuing to use the compressor of the air conditioner (1250).

[0328] In some embodiments the determination whether the cost of electricity rises specifically determines of if cost of electricity rises due to phase drift.

[0329] It is noted that such a response to frequency drift or phase imbalance can potentially occur within seconds, and potentially last for a period of seconds, minutes and even hours.

[0330] In some embodiments a method is provided to mitigate electricity costs caused by load imbalance of the electric grid and/or by available supply capacity relative to load demand. In some embodiments the method includes monitoring cost of electricity from a power company, and ordering chillers and or compressors used by a Thermal Energy System (TES) to turn off at times when cost of electricity rises, optionally using a TES system to replace a chiller's compressor can reduce electrical power consumption, and avoid paying for electricity at high-electricity-cost times. In some embodiments, a signal coming from a grid operator is optionally used to trigger removing the electric load of the compressor of the chillers of the TES and/or by removing other chillers in the system and replacing the chillers with the TES stored energy.

[0331] Smart Balancing of Energy Storage and Consumption

[0332] In some embodiments a controller is used to plan a smart balance of energy storage and energy consumption.

[0333] There is a cost involved in consuming energy from an electric grid. Electricity consumption from a grid involves varying parameters, such as, by way of a non-limiting example, cost of the electricity consumption from the grid as a function of time. Such cost may vary over a daily cycle and be different on a weekend or even holidays. Such cost may be retrieved by receiving a transmission of the cost from a power supply company, or by receiving a transmission of a schedule of the cost from the power supply company.

[0334] There is a cost involved in storing energy. By way of a non-limiting example there is a cost to freeze an ice brick.

[0335] By monitoring total power demand of a facility, a control system can identify events when the facility's profile of electric consumption are experiencing spikes and might penalize a customer with high electricity demand costs. In some embodiments the control system optionally identifies the increased demand as a demand that will last only for a short time and the control system calculates or monitors that there is enough available energy storage to mitigate the spikes. In some embodiments, detecting and monitoring the spikes is optionally done by monitoring a building's electricity meter.

[0336] In some embodiments a control system monitors a rate of change in electric demand in a facility and optionally determines predicted electricity demand and/or predicted electricity cost. The control system optionally controls using energy from the electric power supply company or using energy from a TES based on the electricity demand and/or predicted electricity cost. In some embodiments the prediction is optionally based on using a prediction algorithm. In some embodiments the prediction algorithm is optionally based on past load behavior of the facility.

[0337] In some embodiments the control system optionally predicts when electric power consumption will reach or exceed what threshold and/or for what period of time the electric power consumption will reach or exceed what threshold.

[0338] In some embodiments, the control systems monitor an electric meter which measures electric power usage of a facility or building, including power usage of a TES system and power usage of other system at the facility. Electric cost at such a facility may be based on total electric cost, including both the TES system and the other, non-TES systems at the facility. Methods for saving electric cost, saving CO2 emissions, and controlling peak electric demand which are described herein optionally apply to total cost, to cost of operating the TES system by itself, and to various combination including TES and just some of a facility's electric power consuming systems.

[0339] By monitoring total power demand of the facility, the control system potentially identifies events when the facility is approaching an electrical consumption level which will trigger load demand charges which can be very high due to a short peak period. The control system optionally calculates an anticipated gain of cutting an anticipated peak demand value. In some embodiments, a quick reaction to anticipated short peak periods is enabled by a system as described herein. Such a quick reaction may optionally be in addition to, and may be different than, a scheduled load shifting which is typically bases on a difference in energy costs which are optionally used to determine to charge a TES at low energy cost periods and discharge the TES at high energy cost periods.

[0340] Some example system limitations can be distribution limitation of a local grid and load limitation of a facility itself (leads, control and safety breakers and metering devices)

[0341] In some embodiments such a cost is known and/or estimated, and entered into a control program for smart balancing of energy storage and energy consumption.

[0342] In some embodiments a controller measures electric consumption, and calculates an energy cost to freeze a specific amount of ice bricks.

[0343] In some embodiments the controller measures environmental parameters, such as temperature of the environment during freezing, humidity, time-of-day, sun or shade, precipitation, and so on.

[0344] In some embodiments a control program optionally calculates a dependency of cost of storing energy based on the capacity of ice bricks and/or stored energy left from previous days and/or one or more environmental variables. In some embodiments a control program optionally produces a Look Up Table illustrating a dependency of cost of storing energy based on the capacity of ice bricks and optionally based on values of one or more of the measured environmental parameters.

[0345] In some embodiments a control program gathers information and signals from various energy and electricity storage systems in a facility, optionally in addition to information related to the TES system's cold thermal energy storage, and optionally triggers a charging or discharging process of the TES system based on a calculated savings or on a total electricity consumption load shifting, optionally used to support business operations.

[0346] Some of the cost involved with storing energy is related to energy loss over time. Energy stored in ice bricks may be lost, at a rate based on insulation of the ice bricks or the TES system, or on the ice bricks or TES system being in shade or in sunlight.

[0347] There is a cost involved in retrieving stored energy. By way of a non-limiting example there is a cost to circulate fluid through a TES.

[0348] In some embodiments such a cost is known and/or estimated, and entered into a control program for smart balancing of energy storage and energy consumption.

[0349] In some embodiments a controller measures electric consumption, and calculates an energy cost to retrieve a specific amount of energy.

[0350] In some embodiments the controller measures and/or receive from a public or a dedicated data center, environmental parameters, such as temperature of the environment during energy retrieval, humidity, time-of-day, sun or shade, precipitation, and so on.

[0351] In some embodiments a control program optionally calculates a dependency of cost of retrieving energy based on the capacity of ice bricks and one or more environmental variables. In some embodiments a control program optionally produces a Look Up Table illustrating a dependency of cost of retrieving energy based on the capacity of ice bricks and optionally based on values of one or more of the measured environmental parameters.

[0352] In some embodiments a control program optionally calculates a cost of storing energy, compares the cost of storing energy to the cost of energy from the electric grid, and optionally initiates storing energy when the cost of storing energy is less than the cost of the grid energy.

[0353] In some embodiments a control program optionally calculates a cost of storing energy plus a cost of retrieving the energy, compares the cost of storing-and-retrieving energy to the cost of energy from the electric grid, and optionally initiates storing energy when the cost of storing-and-retrieving energy is less than the cost of the grid energy.

[0354] In some embodiments a control program optionally calculates a cost of retrieving energy, compares the cost of retrieving energy to the cost of energy from the electric grid, and optionally initiates retrieving energy when the cost of retrieving energy is less than the cost of the grid energy.

[0355] Some example embodiments of smart balancing of energy storage and consumption are described below.

[0356] In an example embodiment, a control program determines that a cost of energy at noon is lower than in the afternoon or evening, for example, at noon solar electricity is at a peak, and in the afternoon air conditioning demand is still high. In such an embodiment the control program optionally controls storing energy at noon, for example by freezing ice bricks, and retrieving energy during the afternoon or evening, for example by using the frozen ice bricks to cool air conditioning system(s).

[0357] In an example embodiment, a control program determines that a cost of energy at night is lower than during the day. In such an embodiment the control program optionally controls storing energy at night, for example by freezing ice bricks, and retrieving energy during the day, for example by using the frozen ice bricks to cool air conditioning system(s).

[0358] The above description is a description of an embodiment of the control program using a prediction of energy demands or energy costs to perform smart balancing of energy storage and consumption.

[0359] In some embodiments the control program uses various types of data to predict required energy demands. Some non-limiting examples of such data include: a weather forecast; cost-of-energy data from a power company, optionally based on a daily or weekly schedule; historical energy costs, optionally associated with time-of-day and/or day-of-week and/or holiday/weekday/weekend.

[0360] It is noted that TES systems as described herein provide relatively lower costs of storing and/or retrieving energy, potentially enabling a control program as described herein to operate when more expensive systems for storing and/or retrieving energy cannot work, or would not save energy or cost.

[0361] In some embodiments the control program predicts future energy requirements, and/or predicts future opportunities for load balancing and/or predicts future opportunities for consuming lower-cost electricity from the grid. The prediction(s) is optionally used to cause storing heat energy in a TES, in preparation for subsequent heat energy retrieval.

[0362] Supporting Electric Vehicles on an Electric Grid

[0363] In some embodiments a load balance of a facility is supported in order to allow charging of electrical vehicles at a rate and during a periods or periods of time. The charging periods may optionally be pre-defined and/or as required in order to limit the facility electrical demand from the grid to a specific system limitation.

[0364] By monitoring the total power demand of a facility, the control system potentially identifies events when the facility is approaching its limitation either in internal or local distribution, and optionally compares cost of electricity for continuing to charge electric cars relative to cost of discharging a TES system. The control system optionally identifies when to charge electric vehicles, when to discharge a TES system, when to charge a TES system, based on total power demand of a facility and on electricity cost according to an electric supplier's cost, which may be linked to time-of-day and/or spikes in electric demand. In some embodiments, the control system calculates a gain of cutting an anticipated peak demand value relative to a saving based on a scheduled load shifting, where the scheduled load shifting is typically based on a difference in energy charge values between the two periods of charging and discharging. In some embodiments, the control system optionally supplies cooling energy to the facility to allow switching off of chillers to reduce electrical load.

[0365] In some embodiments a load balance of a facility is supported in order to enable optionally using electricity stored in electrical vehicles during a periods or periods. The periods when the electric charge of the vehicles is used may optionally be pre-defined and/or as required in order to limit the facility electrical demand from the grid to a specific system limitation.

[0366] Reference is now made to FIG. 12D, which is a simplified flow chart illustration of a method for mitigating electricity costs caused by charging electric vehicles at a facility according to an example embodiment of the invention.

[0367] The method of FIG. 12D includes:

[0368] using a compressor in a refrigerant or heat transfer fluid flow of an air conditioner (1252);

[0369] monitoring cost of electricity from power company (1254); and

[0370] when cost of electricity rises (1256),

[0371] then using a TES system to cool the refrigerant or heat transfer fluid of the air conditioner, thereby lowering electric consumption (1258),

[0372] else (1260) continuing to use the compressor of the air conditioner.

[0373] Reference is now made to FIG. 12E, which is a simplified flow chart illustration of a method for mitigating electricity costs caused by peak electric demand charges according to an example embodiment of the invention.

[0374] The method of FIG. 12E includes:

[0375] using a compressor in a refrigerant flow of an air conditioner (1262);

[0376] monitoring use of electricity at a facility (1264);

[0377] predicting when peak electric demand charges are anticipated (1266); and

[0378] when peak electric demand charges are anticipated,

[0379] then using a TES system to cool the refrigerant of the air conditioner, thereby lowering electric consumption (1268,

[0380] else (1270) continuing to use the compressor of the air conditioner.

[0381] Controlling CO.sub.2 Emissions

[0382] In some embodiments a control program takes into account an amount of CO.sub.2 emissions corresponding to an amount of electric power usage and additional parameters such as time of day and source of the electric power. In some cases cost of electricity is linked to amount of corresponding CO.sub.2 emissions. However, in some cases CO.sub.2 emissions may not correlate directly to cost or may not correlate to cost at all. In some embodiments the control system optionally controls using TES system to lower an energy consumption load of a facility in order to reduce CO.sub.2 emissions. In some embodiments the control system optionally controls using TES system to lower an energy consumption load of a facility taking into account both CO.sub.2 emissions and electric energy cost. In some embodiments the control program measures Co2 emissions as amount of CO.sub.2 consumed per kWh.

[0383] Reference is now made to FIG. 12F, which is a simplified flow chart illustration of a method for mitigating CO.sub.2 emissions caused by electric consumption according to an example embodiment of the invention.

[0384] The method of FIG. 12F includes:

[0385] using a compressor in a refrigerant flow of an air conditioner (1272);

[0386] monitoring CO.sub.2 emissions corresponding to use of electricity at a facility (1274); and

[0387] using a TES system to cool the refrigerant of the air conditioner at high-CO.sub.2 emission periods (1276), thereby lowering CO.sub.2 emissions.

[0388] Controlling Maximum Power Demand

[0389] In some embodiments a control program takes into account a top limit of electric power usage which may be imposed on a facility. The control program optionally measures electric power usage of a facility, and when the facility reaches a top limit value, or reaches a threshold value, when the control program calculates and predicts reaching any of the above-mentioned values, the control program optionally uses energy stored in TES system to take on some of the electric load used for cooling, thereby freeing up some electric load.

[0390] By way of a non-limiting example, in some cases a facility has a top limit of Q (kW or MW) electric power consumption, and provides X electric power for air conditioning, X electric power for various systems, and Z electric power for charging electric vehicles. It is noted that charging electric vehicles takes up a large amount of power. Even a large building may be able to provide charging for 10 electric vehicles, but not for 20. When the control program senses that the top limit is close to being reached, the control program may initiate using the TES system to provide cooling for air conditioning, thereby freeing up electric power consumption of the air conditioning for charging additional electric vehicles.

[0391] Reference is now made to FIG. 12G, which is a simplified flow chart illustration of a method for preventing reaching an upper limit of electric consumption at a facility according to an example embodiment of the invention.

[0392] The method of FIG. 12G includes:

[0393] using a compressor in a refrigerant flow of an air conditioner (1282);

[0394] monitoring use of electricity at a facility (1284); and

[0395] when reaching an upper limit of electric consumption is anticipated (1286),

[0396] then using a TES system to cool the refrigerant of the air conditioner (1288), thereby lowering electric consumption,

[0397] else (1290) continuing to use the compressor of the air conditioner.

[0398] Settings

[0399] In some embodiments, a controller such as the controller described herein is set to provide heat exchange fluid at a temperature higher than −10 degrees Celsius to ice bricks containing water and an ice nucleation agent.

[0400] Providing water at higher temperatures is potentially more efficient. For example, potentially less heat is lost to the environment by providing heat exchange fluid at a temperature closer to the environmental temperature.

[0401] It is noted that ice nucleation agents such as mentioned herein, by way of a non-limiting example such as quartz, enable phase change materials, by way of a non-limiting example, water, to freeze at a temperature higher than conventional systems, for example at a temperature higher than freezing coil systems.

[0402] In some embodiments a structure of an ice brick or array or TES system as described herein together with phase change materials to which ice nucleation agents are added, potentially provides a synergistic effect, of storing energy by phase change more efficiently, and/or at higher temperatures, than conventional systems.

[0403] In some embodiments a structure of an ice brick or array or TES system as described herein together with phase change materials to which ice nucleation agents are added, potentially provides a synergistic effect, of using chiller fluid set to higher temperatures than conventional systems, potentially saving energy and energy costs.

[0404] In some embodiments, the controller is set to provide heat exchange fluid at a temperature of −5 degrees Celsius, and even a temperature of −2.7 degrees Celsius to the ice bricks containing water and the ice nucleation agent.

[0405] In some embodiments, the controller is set to provide heat exchange fluid at a temperature of in a range between −10 degrees Celsius and −2.5 Degrees Celsius, inclusive, to the ice bricks containing water and an ice nucleation agent.

[0406] Above-mentioned International Patent Application Number PCT/IB2018/001091 describes, at least in some embodiments, a system and method for thermal energy storage using configurable ice bricks or thermal energy storage units.

[0407] Reference is now made to FIGS. 1A-1E which are schematic diagrams of a thermal energy storage system according to at least some embodiments of the present invention. As shown, thermal energy storage (TES) system 100 uses the HVAC chiller 102 of an air-conditioning (HVAC) system in an installation. Non-limiting examples of an installation include an office building, residential building, shopping mall, airport terminal, factory, server room or similar. When operating without the system 100 of the present invention, HVAC chiller 102 cools a third fluid 124 which is then circulated throughout the installation for cooling load 130. Third fluid 124 is optionally, water.

[0408] As described above one aim of some embodiments of the present invention is to “store cooling” using the TES 100. Alternatively the same system 100 may be used to store heat. The TES 100 comprises a fluid distribution system 104 which comprises those components necessary for distributing the first fluid 120, second fluid 122 and third fluid 124 throughout system 100. Therefore distribution system 104 comprises one or more pumps 106, piping 108, flow control mechanisms 107 such as valves, and monitoring components 109 for monitoring, for example, temperatures and flow rates inside system 100. Monitoring 109 optionally feeds data to a controller 105 for controlling the freezing and/or cooling process via control of chillers 102 and 150, HE 170, load 130, array 110, and the components of fluid distribution system 104 as described further below. In normal use HVAC chiller 102 cools third fluid 124 which is directed by fluid distribution system 104 from HVAC chiller 102 via pipes 108C to pipes 108L for flow through load 130.

[0409] TES 100 further comprises a thermal storage array 110. Array 110 comprises multiple ice bricks 112. Each ice brick 112 comprises multiple ice capsules 114 surrounded by first fluid 120. Embodiments of ice bricks 112 and ice capsules 114 are described further below with reference to FIGS. 2A-2U and 3. Ice capsules 114 are closed or sealed capsules containing second fluid 122. Second fluid 122 is optionally, water such that exposure of capsules 114 to a low temperature first fluid 120 surrounding capsules 114 results in capsules 114 cooling and in turn second fluid 122 cooling and changing phase into ice.

[0410] First fluid 120 optionally has a lower freezing point than second fluid 122. Non-limiting examples of a first fluid 120 include ethylene glycol, ethylene glycol mixed with water, salt water, or similar fluids. TES 100 further comprises a TES chiller 150 for cooling first fluid 120 to a temperature lower than the freezing point of second fluid 122. TES chiller 150 is one of air-cooled or water-cooled.

[0411] Second fluid 122 is optionally water mixed with an ice nucleation agent. The ice nucleation agent is optionally quartz. The type of quartz used may be any one of but is not limited to: Herkimer Diamond, Rock crystal, Amethyst, Ametrine, Rose quartz, Chalcedony, Cryptocrystalline quartz, Carnelian, chalcedony, Aventurine, Agate, Onyx, Jasper, Milky quartz, Smoky quartz, Tiger's eye, Citrine, Prasiolite, Rutilated quartz, or Dumortierite quartz. Quartz is cheap and easily available and resistant to repeated freezing cycles of the second fluid. Furthermore it raises the required starting temperature of freezing the ice by several degrees. Hence, a nucleation agent improves the efficiency and responsiveness of the thermal energy storage system 100.

[0412] Optionally second fluid 122 comprises strips of a metal floating in second fluid 122 inside capsules 114 and causing even distribution of ice formation inside capsules 114. Optionally, the metal is aluminum. Optionally, the strips are up to 0.5 mm thick. Optionally, the strips are up to 30 cm long, optionally the strips are up to 1 cm wide. This optional aspect is explained in more detail with reference to FIG. 8.

[0413] Each ice brick 112 optionally has a long and narrow form factor as shown in FIGS. 2E to 2H to enable efficient heat transfer between capsules 114 and first fluid 120. An ice brick 112 with a long form factor has optionally a length L that is at least three or four times greater than its maximum width W and/or height H. Bricks 112 can optionally be connected end to end creating long linear modules comprising multiple bricks 112. The modular structure and number of bricks 112 used enables control of the rate of energy being discharged to provide for the exact thermal energy storage needs per installation and also provides for flexible installation options as array 110 can be shaped as required. This optional aspect is explained in more detail with reference to FIGS. 8A and 8B.

[0414] Capsules 114 are optionally spaced slightly apart within bricks 112 to increase the overall ratio between surface area and volume of the second fluid 122 that is to be frozen. Optionally, brick 112 contains between 65% and 85% of second fluid 122. Optionally, brick 112 contains 75% of second fluid 122. Capsules 114 optionally comprise polymers such as polyvinyl chloride or other suitable durable and low cost materials. Capsules 114 optionally comprise protrusions or ridges on their outer surface to provide spacing between capsules 114 for flow of first fluid 120 and for increasing turbulence of first fluid 120.

[0415] In use of system 100 shown in FIG. 1A, TES chiller 150 cools first fluid 120, optionally to a temperature below the freezing point of second fluid 122. First fluid 120 is pumped from TES chiller 150 via pipes 108G and directed by fluid distribution system 104 via pipes 108T through array 110 to freeze second fluid 122 (also referred to herein as a “charging process”). First fluid 120, which has increased in temperature then exits array 110 via pipes 108T and is directed by fluid distribution system 104 back to the pipes 108G to chiller 150 to be cooled again. During the charging process the provision of first fluid 120 may be continuous or non-continuous. The charging process is optionally stopped when a desired temperature of first fluid 120 is reached within one or more bricks 112, or when a predefined time period has lapsed, or when a predefined amount of energy is stored in array 110. A (fully) charged array 110 usually comprises a plurality of capsules 114 with a second fluid 122 in a frozen state.

[0416] Once array 110 has been charged, a cooling process (also referred to herein as a discharge process), is used to cool load 130 using array 110. First fluid 120 inside array 110 is directed via piping 108T to distribution system 104 and through pipes 108S into heat exchanger 170 where first fluid 120 cools third fluid 124. Distribution system 104 then directs cooled third fluid 124 through pipes 108H into pipes 108C to flow through HVAC chiller 102 and then load 130 (via pipes 108L).

[0417] Alternatively third fluid 124 is directed through pipes 108H in parallel to HVAC chiller 102 directly to load 130 via fluid distribution system 104 to piping 108L. Since third fluid 124 has been cooled by first fluid 120 in HE 170, HVAC chiller 102 optionally does not need to be activated, thus producing energy savings. As first fluid 120 circulates between HE 170 and array 110, capsules 114 containing frozen second fluid 122 cool first fluid 120 which then directly or indirectly cools third fluid 124 and load 130. Optionally, the temperature of first fluid 120 entering heat exchanger 170 is between 5 degrees Celsius at the inlet and 10 degrees Celsius at the outlet. As capsules 114 cool first fluid 120, frozen second fluid 122 gradually undergoes a phase change and melts until a point where array 110 is no longer sufficiently cooling first fluid 120 and array 110 is said to be discharged. A (fully) discharged array 110 usually comprises capsules 114 with a second fluid 122 in a liquid state.

[0418] The charging process optionally takes place during off-peak hours (hours in which the load on the electrical grid is low) while the discharge process optionally occurs according to the demands of load 130—even during peak hours. The discharge process is optionally stopped when a cutoff temperature of first fluid 120 is reached, or when a predefined time period has elapsed, or when a predefined amount of energy is output from array 110, or under control of load 130 or when the demand for cooling at load 130 has lowered to a desired level. The direction of flow of first fluid 120 within array 110 during the charging process may be the same, or may differ from the direction of flow of first fluid 120 during the discharge process.

[0419] Alternatively, system 100 is used for heating. For heating TES chiller 150 optionally operates as a heat pump. TES Chiller 150 heats first fluid 120, optionally in off peak hours. First fluid 120 is pumped from TES chiller 150 via pipes 108G and directed by fluid distribution system 104 via piping 108T and through array 110 to warm second fluid 122 (also referred to herein as a charging process). First fluid 120, which has decreased in temperature then exits array 110 and is directed by fluid distribution system 104 through pipes 108T and piping 108G to TES chiller 150 to be warmed again. During the warming process the provision of first fluid 120 may be continuous or non-continuous. The warming process is optionally stopped when a desired temperature of first fluid 120 is reached within one or more of bricks 112, or when a predefined time period has lapsed, or when a predefined amount of energy is stored in array 110, and the like. No phase change takes place in the array.

[0420] Once array 110 has been charged, a warming process (also referred to herein as a discharge process), is used to warm load 130 using array 110. First fluid 120 inside array 110 is directed via distribution system 104 through pipes 108T and 108S into heat exchanger 170 where first fluid 120 warms third fluid 124. Distribution system 104 then directs warmed third fluid 124 from pipes 108H through pipes 108C to flow through HVAC chiller 102 and then load 130 (via pipes 108L). Alternatively third fluid 124 is directed through pipes 108H in parallel to HVAC chiller 102 directly to load 130 via fluid distribution system 104 to piping 108L. Since third fluid 124 has been warmed by first fluid 120 in HE 170, HVAC chiller 102 (functioning as a heat pump) optionally does not need to be activated as third fluid 124 has been warmed thus producing energy savings. As first fluid 120 circulates between heat exchanger 170 and array 110, capsules 114 containing warmed second fluid 122 warm first fluid 120 which then directly or indirectly warms third fluid 124 and load 130.

[0421] The charging process optionally takes place during off-peak hours (hours in which the load on the electrical grid is low) while the discharge process optionally occurs according to the demands of load 130—even during peak hours.

[0422] Monitoring 109 of fluid distribution system 104 optionally comprises one or more temperature monitors for monitoring at least one of: The temperature of first fluid 120 before entering array 110; The temperature of first fluid 120 in any location within array 110; The temperature of first fluid 120 after exiting array 110; The temperature of second fluid 122 within one or more capsules 114; The temperature of one or more ice bricks 112; The temperature of first fluid 120 before entering HE 170; and the temperature of first fluid 120 when leaving HE 170. Additionally or alternatively, monitoring 109 comprises one or more flow monitors (not shown) for monitoring at least one of: The flow of the first fluid 120 before, inside and after array 110; and the flow of first fluid 120 before, inside and after HE 170.

[0423] While FIGS. 1A-1E show single instances of chillers 102 and 150, HE 170, load 130, array 110, and the components of fluid distribution system 104 it should be understood that TES 100 may comprise any suitable number of these components.

[0424] The system 100 of FIG. 1B functions in the same manner as that of FIG. 1A, but the illustrated embodiment comprises an air compressor 140. Compressor 140 draws air 126 from the top of the each of bricks 112. This air 126 is optionally compressed to between 10 and 20 bar resulting in the air 126 heating up as a result of compression. This compressed air 126 is then pumped into the bottom of each of bricks 112 through an air to air heat exchanger 142 and/or an expansion valve (not shown)—dropping to a temperature of between −20 to −30 degrees Celsius. This air 126 is bubbled through each of bricks 112 to further cool the contents before exiting through the top of the bricks 112 at between −5 to +5 degrees Celsius. This cold air 126 is then fed once again into the compressor 140 creating a cooling closed loop 108P. Cooling loop 108P is shown for simplicity as connected directly to thermal storage array 110 but cooling loop 108P is optionally part of fluid distribution system 104 and is controlled as are other piping systems as described herein. In this embodiment second fluid 122 is optionally combined with salt or other suitable material to lower the freezing point of second fluid 122.

[0425] The system of FIG. 1C functions in the same manner as that of FIG. 1A, but where the condensation cycle of TES chiller 150 is water cooled comprises a heat exchanger 152 fed from third fluid 124. In this embodiment load piping 108K is adapted to connect to HE 152 in TES chiller 150. Load piping 108K carries third fluid 124 which has been chilled by HVAC chiller 102—typically to a temperature between but not limited to 7 to 12° C.

[0426] TES chiller 150 then cools first fluid 120 via HE 154 to a temperature below the freezing point of second fluid 122 such that first fluid 120 may be pumped through array 110 to freeze second fluid 122 inside capsules 114. The discharging process then takes place in HE 170 as for other embodiments. This arrangement increases the energy efficiency of TES chiller 150 which can utilize the abundant supply of cooled third fluid 124 available when load 130 is partially or entirely not being used for example but not limited to nighttime usage in an office complex. HVAC chiller 102 optionally, cools third fluid 124 at night when the outside temperature is lower and electricity costs are lower for more effective and cheaper energy usage. Since water cooled TES chiller 150 is more efficient it can also be smaller than in other embodiments where an air-cooled chiller is used.

[0427] The system of FIG. 1D combines the functionality of FIGS. 1B and 1C to provide for a TES chiller 150 connected to third fluid via HE 152 that is supplemented by compressive cooling from air compressor 140.

[0428] The system of FIG. 1E functions in the same manner as that of FIG. 1A, but in the illustrated embodiment some or all of ice bricks 112 do not comprise capsules 114. In the embodiment of FIG. 1E TES 100 is used to store first fluid 120 in ice bricks 112. Thus first fluid 120 is cooled by chiller 150 and this cooled first fluid 120 is then pumped into ice bricks 112 for storage and use for cooling third fluid (via HE 170) at other times. As above, non-limiting examples of a first fluid 120 include ethylene glycol, ethylene glycol mixed with water, salt mixed with water, or other combinations of these or other fluid to form “slushes” or similar fluids.

[0429] Reference is now made to FIGS. 2A-2U which are illustrations of ice bricks, ice capsules and thermal storage arrays according to at least some embodiments of the present invention. FIGS. 2A-2D show preferred embodiments of capsules 114. Capsule 114 comprises a filling nozzle 202 placed on an upper corner of capsule 114 to enable filling of capsule 114 to a maximum with second fluid 122 while still enabling efficient packing of capsules 114. Capsules 114 optionally comprise narrow-side spacers 204 and broad-side spacers 206. When provided, spacers 204 and 206 create a gap between capsules 114 when these are packed together inside brick 112. This gap is required to allow flow of first fluid 120 between capsules 114 for freezing of second fluid 122 inside capsules 114. Capsules 114 comprise a high ratio of depth D vs. length L and height H to create a greater surface area around a thinner piece of ice for a more efficient heat transfer of second fluid 122).

[0430] FIGS. 2E-2H show preferred embodiments of ice bricks 112 comprising capsule 114. Ice brick 112 comprises a rectangular enclosure 220 for enclosing multiple capsules 114. Capsules 114 are packed together to maximize the amount of second fluid 122 that is contained inside brick 112. Brick is equipped on each end with alignment or support panels 227 for aligning capsules 114 and sealing brick end panels 226 such that brick 112 is watertight when sealed. Brick 112 is connected to array 110 via inlet/outlet pipes 224. Mounting brackets 222 are provided for mounting brick 112 in a fixed position in the array 110 as further described below. Aside from inlet/outlet pipes 224 and interconnecting piping 228 used to connect bricks, brick 112 is completely sealed to fully contain first fluid 120 that flows through brick 112.

[0431] Optionally, brick 112 has a size of 50×50×400 cm. Optionally, brick 112 has a volume of 1000 L comprising 75% (750L) of second fluid 122. Optionally, brick 112 has an energy storage capacity of 19.8 trhl69 kWh. Alternatively, brick 112 has a size of 25×25×400 cm. The size of brick 112 is selected to provide a balance between sufficient energy storage and construction modularity of the array.

[0432] FIGS. 2I-2N show preferred embodiments of bricks 112 in flexible configurations of thermal storage arrays 110. Brick 112 is used as a building block for configuration of an array 110 that is of any desired layout and also capacity. As shown in FIGS. 2I and 2J, bricks 112 are stacked on top of one another, laid end to end and also laid next to one another. Inlet/outlet pipes 224 and interconnecting piping 228 are then used to provide fluid connection between the bricks 112 in the array for first fluid 120. Bricks 112 are fluidly connected in parallel or alternatively in series or alternatively a combination of parallel and series connections.

[0433] As shown in FIGS. 2K-2N, once the array 110 has been built with a desired capacity (number of bricks 112), and form (arrangement of bricks 112), insulation panels 230 are attached to the outer surface of the array 110 to fully insulate the array and preserve the thermal storage within the bricks 112. This configuration saves on the total insulation needed as only the outer surface of the complete array 110 needs to be insulated, and not every surface of every brick 112. Array 110 is optionally assembled on top of base frame 232 which is optionally insulated on its underside.

[0434] Once array 110 has been arranged into the desired form such as the rectangular box of FIG. 2M or the planar platform of FIG. 2N or any combination of these to create any structural arrangement required for the specific installation, this form can be integrated into the structure served by the thermal storage system 100. As a non-limiting example, the platform of FIG. 2N could function as a floor or could be erected vertically to function as a wall or could function as both floor and wall or could function as a raised platform inside, next to, or on the building/structure serviced by the TES system 100.

[0435] FIGS. 2O-2R show additional preferred embodiments of ice bricks 112 comprising capsules 114, wherein capsules 114 are narrower in a middle section thus creating gaps between capsules 114 for flow of first fluid 120.

[0436] FIGS. 2S-2U show additional preferred embodiments of capsules 114, wherein capsules 114 comprise a widened middle with a supporting ridge 250 so that upper part 256 and lower part 254 do not collapse when ice forms inside capsule 114. Ridge 250 and ridges 252 create a gap between capsules 114 when these are packed together inside brick 112. This gap is required to allow flow of first fluid 120 between capsules 114 for freezing of second fluid 122 inside capsules 114. Capsules 114 also comprise protrusions 260. Protrusions 260 increase the Reynolds number for first fluid 120 outside capsules 114 thus resulting in a more turbulent flow of first fluid 120 and therefore better distribution of ice formation inside capsule 114.

[0437] FIG. 2V shows a side view of a capsule 114 with protrusions 260, a ridge 252 and a filing nozzle 202. The filling nozzle is placed such that it does not increase beyond the general outer shape of the rectangular shaped capsule 114. FIG. 2W shows the capsule of FIG. 2V in another side view, perpendicular to the view of FIG. 2V. FIG. 2X shows the capsule of FIGS. 2V and 2W in a front view, wherein the broad-side of the capsule 114 and the general flow direction 290 of the first fluid 120 is shown. The capsule 114 has protrusions 260 that are arranged such that the flow path of the first fluid 260, which passes by the capsule 114, is provided in a meander pattern 291 (or a serpentine pattern). A meander pattern 291 in the sense of the invention is characterized in that the direction of the flow is repeatedly changed. Optionally, the meander pattern 291 is characterized in that the direction of the flow is regularly changed. Even more preferred is that the meander pattern is approximately symmetrical around a center line at least in a part of the meander pattern. The reference numeral 292 refer to flat areas of the capsules 114 between the protrusions 260. FIG. 2Y shows a perspective view of the capsule 114, which is shown in FIGS. 2V, 2W and 2X.

[0438] Reference is now made to FIG. 3 which shows an ice capsule according to at least some embodiments of the present invention. As shown in FIG. 3, capsule 114Cy is optionally provided in a cyclohexane shape. In use, multiple cyclohexane shaped capsules 114Cy are placed inside brick 112 to freely settle inside brick 112. Thus capsules 114Cy are not fixed inside brick 112. The irregular shape of cyclohexane shaped capsules 114Cy enables a high packing factor within brick 112 while allowing gaps for flow of first fluid 120 around capsules 114Cy for freezing the second fluid 122 inside them. Moreover, also a plurality of cyclohexane-shaped capsules 114Cy provides defined flow paths inside the brick 112C, since such defined cyclohexane-shaped capsules 114C will create a defined geometric pattern of these capsules 114c when placing a plurality of them inside an enclosed volume.

[0439] Reference is now made to FIG. 4 which shows a cylindrical Ice brick according to at least some embodiments of the present invention. In the optional embodiment as shown in FIG. 4, ice brick 112C is cylindrical and comprises capsules 114C arranged in one or more arrays. Optionally there are multiple arrays placed at different heights within brick 112C. Optionally, the cylindrical brick 112C is adapted to be positioned underground. Brick 112C is manufactured from a pipe comprising a spiral metal reinforcement (not shown) than runs along the outside of brick 112C to enable placement of brick 112C underground. The volume of ice brick 112C is optionally between 100-10,000 cubic meters.

[0440] Reference is now made to FIG. 5A which shows a TES system capable of activating separate subsets of ice bricks by a controller, FIG. 5B which shows a flow diagram for operation of a TES system, and FIG. 5C which shows experimental data from operation of a TES system according to at least some embodiments of the present invention. As shown in FIG. 5A, TES system 100 is structured and operates as per TES system 100 of FIG. 1A. Optionally any of the embodiments of FIGS. 1A-1E may be used as described with reference to FIG. 5B. In the embodiment of FIG. 5A, system 100 comprises N ice bricks 112 where N is an integer greater than 2. It should be appreciated that, as described above, array 110 optionally comprises as many ice bricks 112 as are needed to provide sufficient thermal energy storage. Ice bricks 112 are interconnected using inlet/outlet pipes 224 and interconnecting piping 228 and further are interconnected using components of fluid distribution system 104. Flow control 107 of fluid distribution system 104 enables segmentation of array 110 into subsets 520 of ice bricks 112 that can be activated individually as described below.

[0441] As above first fluid 120 flows through ice bricks 112 for charging and discharging. In the discharging process 500 of FIG. 5B, in step 501, the discharging process is initiated. The steps of process 500 are optionally controlled by controller 105 that controls the components of system 100 as described above. Activation of the discharging process may involve several steps such as but not limited to activating pumps 106, opening or closing valves in flow control 107, and monitoring temperatures and flow rates of fluids 120, 122, and 124 using monitoring 109.

[0442] In step 502 as part of the activation process, controller 105 activates a first subset 520A of ice bricks 112 and first fluid 120 is pumped only through this first subset 520A and not through any other ice bricks 112. As shown in FIG. 5A first subset 520A includes ice bricks 112A and 112B, however any number of ice bricks 112, and even a single ice brick 112, may be included in a subset and the example of two ice bricks 112 in a subset 520 should not be considered limiting. Optionally more than one subset 520 is activated in step 502. As first fluid 120 passes through first subset 520A, first fluid 120 is cooled while second fluid 122 is warmed. In step 503, the temperature of first fluid 120 is monitored such as by monitoring 109 as it exits array 110. Optionally temperatures of other fluids in system 100 are also measured in step 503.

[0443] In decision step 504, monitoring 109 indicates whether the monitored temperature has risen above a defined threshold. If the monitored temperature does not exceed the threshold then no action is taken by controller 105 and step 503 of monitoring is continued. When monitoring 109 indicates that the temperature has risen above the defined threshold (which is optionally defined in controller 105) the implication is that second fluid 122 passing through subset 520A is no longer being sufficiently cooled by subset 520A since second fluid 122 of subset 520A has risen in temperature. In a non-limiting example, where the temperature of first fluid 120 has risen above 5 degrees Celsius at the outlet of array 110, subset 520A is no longer sufficiently cooling first fluid 120.

[0444] In decision step 505 controller 105 checks whether all subsets of ice bricks 112 have been activated. When it is determined that not all subsets of ice bricks 112 have been activated, controller 105 activates a next subset 520B of ice bricks 112 in step 506. As above while FIG. 5A shows subset 520B including only ice bricks 112C and 112D, this should not be considered limiting and subset 520B could comprise any number of ice bricks 112. Subset 520B is optionally activated in addition to subset 520. Alternatively subset 520 is deactivated when subset 520B is activated. Optionally more than one subset is activated in step 506. The activation of subset 520B results in a decreased temperature as monitored by monitoring 109 in step 503.

[0445] Steps 503, 504 and 505 are repeated as shown in FIG. 5B until it is determined in step 505 that all available subsets, up to subset 520N, of ice bricks 112 have been utilized and in step 507 the discharge process 500 is stopped.

[0446] FIG. 5C shows experimental data from operation of a TES system. As shown in the graph of FIG. 5C, the temperature of first fluid 120 is monitored at the outlet of array 110 and plotted as line 532 as a function of time elapsed since activation of a discharging process. In the experimental system, three ice bricks 112 were activated at time=0 and as shown, the temperature increased from −5 degrees Celsius to around 5 degrees Celsius at the time indicated at point 530. At time 530, another ice brick was activated in addition to the initial three ice bricks and this immediately lowered the outlet temperature as in graph 532 to around 0 degrees Celsius. The temperature then gradually rose once more to around 5 degrees Celsius as the fourth ice brick also discharged. As can be seen from the experimental graph 532, the gradual activation of ice bricks 112 or subsets of ice bricks 520 results in more balanced discharging of TES system 100, longer discharging time resulting in longer periods of TES cooling of a load 130, and better utilization of each ice brick 112 which is more fully discharged.

[0447] Reference is now made to FIGS. 6A-6G which show spacers for use in an ice brick according to at least some embodiments of the present invention. Spacers 600 and 620 are inserted between capsules 114 inside ice bricks 112. An ice brick 112 optionally comprises multiple spacers 600 or alternatively spacers 620.

[0448] Alternatively an ice brick 112 comprise a combination of spacers 600 and 620.

[0449] FIGS. 6D and 6E show two capsules 114 without any spacer 600 or 620 in a discharged (FIG. 6D) and charged (FIG. 6E) state. FIGS. 6F and 6G show two capsules 114 with spacer 620 in a discharged (FIG. 6F) and charged (FIG. 6G) state. Two capsules 114 are shown for purposes of simplicity and it should be apparent that any number of capsules and spacers may be provided as required inside brick 112. The purpose of spacers 600 and 620 is to maintain a minimum flow area 630 around capsules 114. Flow area 630 is required since capsules 114 expand (FIG. 6E) when capsules 114 are fully charged (second fluid 122 such as water has changed into ice). This expansion by capsules 114 can block the flow of first fluid 120 by constricting flow area 630 (FIG. 6E) preventing first fluid 120 from passing through ice brick and 112 and thereby preventing efficiently cooling of first fluid 120. Further, when second fluid 122 (such as water) is in a discharged state (FIG. 6D) capsules 114 shrink and the flow area 630 between capsules 114 grows causing a significant decrease in first fluid flow velocity which effects heat transfer for both charging and discharging.

[0450] In the embodiment of FIG. 6A spacer 600 ensures a sufficient flow area 630 by fitting between capsules 114 such that capsules 114 cannot expand to fill the flow area. Holes 604 in spacer 600 allow for flow of first fluid 120. When capsules 114 discharge, flexible flaps 602 open away from spacer 600 in order to occupy flow area 630 and thereby increase first fluid flow velocity.

[0451] In the embodiment of FIGS. 6B, 6C, 6F and 6G, spacer 620 ensures a sufficient flow area 630 by fitting between capsules 114 such that capsules 114 cannot expand while freezing to fill flow area 630. FIG. 6C shows cross section A′-A′ of spacer 620. Gaps 624 between the vertical bars 621 and horizontal bars 622 in spacer 620 allow for flow of first fluid 120. As shown in FIG. 6F spacer 620 fits between capsules 114 and vertical bars 621 and horizontal bars 622 increase the flow velocity of first fluid through flow area 630. As shown in FIG. 6G, when capsules 114 are charged and expand, spacer 620 prevent capsule 114 from blocking flow area 630 thus ensuring continued flow of first fluid 120 around capsules 114.

[0452] Reference is now made to FIGS. 7A to 7D, which show an ice brick 112, i.e., a thermal energy storage unit 711.

[0453] The thermal energy storage unit 711 of FIG. 7A comprises a tube 712, which has the shape of an elongated, hollow body. The tube 712 is optionally made of metal, e.g., carbon steel or stainless steel. A front end element 713A and a back end element 713B are arranged to close the tube at both ends such that a rectangular-shaped enclosure is provided. Both elements 713A and 713B are also optionally made of metal, e.g., stainless steel or carbon steel and provide means for mounting the thermal energy storage unit 711 e.g. to supporting means (not shown). The front end element 713A and the back end element 713B have an inlet 714A and an outlet 714B, respectively. The inlet 714A and the outlet 714B can be connected to further thermal energy storage units 112, the piping 10 and/or to the fluid distribution system 104. Inside the tube 712, a plurality of capsules 715 is arranged. The capsules 115 have the shape of plates or bricks. Furthermore, the capsules 715 have a concave or recessed shape of their main surfaces (i.e. of their broad-sides). The arrangement of the capsules 715 inside the tube is optionally configured by a plurality of horizontally arranged stacks 717 of capsules 715 (i.e., the stacks are stacked in a width direction of the tube 712). For example, 16 or 8 capsules 715 can form one stack 717 of capsules 715. A plurality of stacks 717 is arranged one after another along the length of the tube 712. The capsules contain a phase-change material as second fluid 122 such as water, and preferable a nucleation agent, such as quartz. Between the capsules 715, as well as between the capsules and the tube 712, a space 716 is provided, in which the first fluid 120, e.g., a water/glycol mixture, can flow inside the tube 712 from inlet 714A to outlet 714B.

[0454] This arrangement allows an efficient exchange of heat between the first fluid 120 and the second fluid 122 via the wall of the capsule 715. The actual heat exchange rate between the capsule 715 and the first fluid 120 is dependent on several factors including the speed of the flow, the effective area of the contact surface between the flow of the first fluid 120 and the capsule 715, and the type of the flow (e.g., turbulent or laminar). The embodiment of FIG. 7A improves all of these factors. This is explained in more detail below:

[0455] The elongated shape of the tube in combination with the stacked arrangement of the capsules 715 defines residual free spaces 716, which result in a plurality of predefined flow paths 718 of the first fluid next to the capsules. The overall flow of the first fluid 120 at the inlet 714A is divided into the plurality of predefined flow paths 718, wherein each of the flow paths 718 passes by a plurality of capsules along the length of the tube 712. Moreover, the capsules 715 are configured such that the flow paths 718 are defined in a frozen (expanded) state of the capsules 715 as well as in a non-frozen (non-expanded) state of the capsules 715. In other words, a plurality of predefined or fixed flow channels for the first fluid 120 is provided between the capsules 715 while considering the changing volume of the capsules due to the volume change of the second fluid, especially while changing phase. Consequently and in contrast to conventional tank-based thermal energy storage units, a predefined system of a plurality of flow paths 718 for the first fluid 120 for exchanging heat is provided. The flow of the heat transfer fluid in conventional tank based thermal energy storage units has a high degree of randomness, wherein for example it is hard for the first fluid to reach edges of the tank.

[0456] Moreover, the plate shape of the capsules 715 geometrically increases the surface of the capsules 715 (i.e., its surface-to-volume ratio), wherein the largest surfaces (i.e. the broad-sides) of the capsules 715 advantageously define its main surfaces for exchanging heat.

[0457] Correspondingly, each flow path 715 of FIG. 7A has a narrow shape that is aligned parallel to said main surfaces of the capsules 715. The narrow shape of defined flow paths 718 utilizes the main surfaces of the capsules 715 such that the heat transfer rate is increased. In other words, the above explained arrangement of the thermal energy storage unit 711 significantly increases the effective area of the contact surface for exchanging heat while keeping the pressure drop at an acceptable level (e.g., below 1 bar).

[0458] The elongated shape of the tube 712 provides defined flow paths of the first fluid 120 that are significantly longer than with conventional systems. Hence, the exchange of heat of the first fluid 120 with the plurality of stacks 717 is optimized, since a gradual activation of the stacks 717 while frosting or defrosting the capsules 715 takes place.

[0459] Additionally, the average length of the flow paths is increased to be longer than the length L of the tube 712. This additionally increases the heat transfer rate.

[0460] FIG. 7B shows a cross-section of an empty tube 712. FIG. 7C shows a cross-section of a tube 712 including a stack 717 of capsules 715 with water in a liquid (non-frozen) state. Hence, the thermal energy storage unit 711 of FIG. 7C is fully discharged. FIG. 7D shows a cross-section of a tube 712 including a stack 717 of capsules 715 with water in a frozen/solid state. Hence, the thermal energy storage unit 711 of FIG. 7D is fully charged. The tube 712 of FIG. 7B has ideally an overall cross-section (i.e. cross-sectional area) of the tube 712A for the first fluid 120, if considered without any capsule 715. If a stack 717 of capsules 715 is placed inside the tube 712, narrow-shaped flow paths are provided between capsules 715; in FIG. 7C one of these narrow flow paths 718 is indicated by a plurality of circles, which indicate the flow direction of the first fluid 120. The flow paths 718 are provided in a cross-sectional area between each of two capsules 120 (one of these free-flow cross-sectional areas for the flow paths is indicated with the reference numeral 718A in FIG. 7C) for the first fluid 120 and, at the left and right side of FIG. 7C, between the wall of the tube 120 and the outmost left and right capsule 715, respectively. One of these cross-sectional areas that define the flow paths 718 is indicated with the reference numeral 718A in FIG. 7C. FIG. 7D shows almost the same configuration as FIG. 7C with the key difference that the residual cross-sectional areas for the flow of the first fluid 120 between the capsules 715 are smaller, since the capsules 715 are expanded by the frozen second fluid 122 inside them. One of these free-flow cross-sectional areas that define the flow paths 718 for the first fluid 120 is indicated in FIG. 7D by the reference numeral 718B. The plurality of stacks 717 is arranged such that continuous flow paths 718 are provided along the length of the tube in general from the front end to the back end to the tube. The average length of these flow paths 718 is longer than the length of the tube 712 itself. Optionally, the stacks 717 of the capsules 715 have the same number of capsules 715. Optionally, the stacks 717 are consecutively arranged next to each other such that the flow paths 718 are provided by the plurality of stacks 717 itself.

[0461] Since water expands its volume while charging/freezing, the capsules 715 of FIG. 7C require more space than the capsules of FIG. 7B. This effect is also called “breathing-effect” of the capsules 715. Due to this breathing effect, the residual space for the first fluid 120 changes according to the state of the second fluid 122 inside the capsules 715. The breathing-effect of the capsules 715 has to be considered while defining the flow paths 718. First, the stacks 717 have to be adapted such that the flow paths 718 are not blocked in the charged and in the discharged state. Second, the stacks 717 have to be adapted such that the flow paths 718 provide an acceptable pressure drop in the case of frozen capsules 715 as well as in the case of non-frozen capsules 715. Third, the overall thermodynamic configuration of the thermal energy storage unit 711 has to be optimized. This includes especially the flow dynamics of the first fluid 120 in the flow path 718 that should be configured such that an efficient heat transfer between the capsules 715 and the first fluid 120 can take place.

[0462] The first item mentioned above is for ensuring that a flow of the first fluid 120 can be provided at all times.

[0463] The second item mentioned above is explained more in detail as follows. The longer the flow path and smaller the flow path's cross-sectional area, the greater is the increase of the pressure drop. An increased pressure drop has the disadvantage of a higher pumping power consumption (i.e., higher system losses and less total efficiency of the system) and the disadvantage of increasing mechanical requirements for the whole system. Consequently, the pressure drop from inlet 714A to outlet 714B has to be below 1 bar (atmosphere). Optionally, thermal energy storage unit is configured such that the pressure drop is less than 0.5 bar in its fully-charged as well as in its fully-discharged state.

[0464] With respect to the third item mentioned above, a ratio of a combined length of a plurality of tubes (or one very long tube) to a flow-cut-area is in a range of about 40 to 200, optionally of about 60 and 150. These ratios of a flow-cut-area to a combined length of a plurality of tubes (i.e., the total length of several tubes 712 connected together in series) provide an efficient heat transfer rate with an acceptable pressure drop.

[0465] This allows on one hand more time for the capsules placed closest to the inlet (which suffer from reduced heat transfer rate due to ice melting inside the capsules) to continue their heat transfer into the first fluid 120 at a lower heat transfer rate and a lower exchange temperature, while the capsules 715 located more downstream of the flow of the first fluid 120 continue their heat transfer at a higher heat transfer rate.

[0466] The term “flow-cut-area” is a number which is calculated as follows:


AFFCAp=(TCSA−(CCSA-LS+CCSA-FS)/2×CPS)/CPS

[0467] wherein the above stated variables are defined as follows:

[0468] AFFCAp=Average free flow-cut-area per capsule

[0469] TCSA=overall available cross-sectional area 712A of the tube (see FIG. 7B);

[0470] CCSA-LS=capsule cross-sectional area 715 in the liquid state of the second fluid (i.e. in a discharged state, see FIG. 7C);

[0471] CCSA-FS=capsule cross-sectional area 715 in the frozen state of the second fluid (i.e. in a charged state, see FIG. 7D);

[0472] CPS=number of capsules 715 installed in parallel.

[0473] With the above stated formula, an average free flow cross-sectional area (i.e., (AFFCAp) per capsule 715 is used to calculate the available total flow area in a tube's cross-section. The result is then used to calculate the average cross-sectional flow area per capsule, i.e., the flow-cut-area.

[0474] The calculated flow-cut-area can be used to calculate a ratio gamma that is a good indicator for the efficiency of the heat transfer between capsule and first fluid as follows:


Ratio gamma=combined length of the plurality of tubes/flow-cut-area (cm/cm.sup.2)

[0475] A gamma ratio of the combined length of the plurality of tubes to the said flow-cut-area of approximately 150 is an optimal value. A system which has been configured according to the above explained requirement demonstrated a yield value (a percentage of second fluid melted during a 4 hours period discharge rate) higher than 80% with an acceptable exit temperature of the first fluid below 5 degrees Celsius and an acceptable pressure drop (˜0.5 bar). Increasing the ratio to 200 (with a shape of the capsule according to the above explained embodiments) will increase the pressure drop beyond the desired limit. Decreasing the ratio below 40 will decrease the yield percentage while discharging to 50%. A ratio in the range of 60 to 90 will also result in a reasonable efficiency of the unit 711. Moreover, the embodiment provides, in contrast to conventional “encapsulated ice” systems, a flat and stable discharge curve (behavior).

[0476] It is to be noted that the above stated rages and optimal values for the ratio gamma are the result of theoretical and practical experiments with the above embodiments.

[0477] FIG. 8A shows a capsule 114 with a filling nozzle 202 that has a predefined diameter. Flat metal strips 801 are provided such that they are arranged inside the capsule 114. The width of the strips is adapted to the diameter of the filling nozzle 202 such that the strips can be inserted into the capsule 114. It is to be noted that the strip 801 that is placed in the filling nozzle 202 in FIG. 8A is only shown for demonstration purposes. The capsule 114 as finally used for the heat storage unit is only provided with strips 801 that are completely located in the interior of the capsule 114. The length of the strips 801 is preferable dimensioned such that they fit well inside the length of the capsule 114. In this way, the strips 801 will stay in place in the interior of the capsule 114 and will effect a large part of the internal volume of the capsule 114. Optionally, a plurality of metal strips is used in order to increase the overall heat transfer efficiency of the capsule 114. These strips 801 act as heat transfer elements, which improve the transfer of heat inside the capsule 114 and improve the total heat transfer efficiency of the individual capsule.

[0478] FIG. 8B shows a capsule 114 with a filling nozzle 202 that has a predefined diameter. Helical flat metal strips 802 are provided such that they are arranged inside the capsule 114. The width of strips is adapted to the diameter of the filling nozzle 202 such that the strips can be inserted into the capsule 114. It is to be noted that the strip 802 that is placed in the filling nozzle 202 in FIG. 8A is only shown for demonstration purposes. Helical flat metal strips 802 provide an even better distribution of heat in the interior of the capsule 114.

[0479] FIG. 9A shows a rigid spacer 620 having vertical bars 621, horizontal bars 622 and gaps 624 between the bars. The rigid spacer 600 is provided between two neighboring capsules 114. Reference is made to FIGS. 6B and 6C and the corresponding explanation. This rigid spacer could, for example, be used in combination with the embodiment described in context with FIG. 7.

[0480] When the capsule's wall deflects towards the neighboring capsule wall while charging (i.e., while freezing of the second fluid 122), the horizontal bars 622 maintain a free flow path near them, which will allow parallel flows 650 of the first fluid 120, which will cause melting of the ice across the whole capsule width. The perpendicular vertical bars will create turbulent flow which will improve the heat transfer coefficient between the wall of the capsule and the flow of the first fluid 120, as depicted by the curved arrows 640.

[0481] FIG. 9B shows a flexible spacer 600 having flaps 602. The flexible spacer 600 is provided between two neighboring capsules 114. Reference is made to FIG. 6A and the corresponding explanations. Furthermore, protrusions 603 are provided in order to create a more turbulent flow. This flexible spacer 600 could, for example, be used in combination with the embodiment described in context with FIG. 7.

[0482] The placement of flexible spacers 600 equipped with flaps 602, which are preloaded to press against the neighboring capsule's 114 flat walls, will force the first fluid to flow through the narrow gap between the capsules' 114 walls. This increases the heat transfer rate of the first fluid 120 with the capsule 114. Additionally the turbulence of the flow is increased. This is depicted by the lines 900 in FIG. 9B. The minimum clearance in the charged stage (i.e., the minimal size of the gap) should be approximately 1 mm on each side.

[0483] Furthermore, the flexible spacer 600 can be configured such that the gap will grow (due to ice melting) to approximately 3 to 5 mm on each side. This which will advantageously cause a reduction of the velocity of the fluid flow of the first fluid 120 to one fourth (¼) of its maximum velocity in the tube.

[0484] The flaps (wings) which are pre-set to expand away from the straight sheet and to move toward the capsule wall and to maintain narrow flow gap for the first fluid 120 near the capsule 114 and will prevent the degradation of performance as described above.

[0485] It is expected that during the life of a patent maturing from this application many relevant air conditioners, chillers and TES systems will be developed and the scope of the terms air conditioners, chillers and TES systems is intended to include all such new technologies a priori.

[0486] As used herein with reference to quantity or value, the term “about” means “within ±20% of”.

[0487] The terms “comprising”, “including”, “having” and their conjugates mean “including but not limited to”.

[0488] The term “consisting of” is intended to mean “including and limited to”.

[0489] The term “consisting essentially of” means that the composition, method or structure may include additional ingredients, steps and/or parts, but only if the additional ingredients, steps and/or parts do not materially alter the basic and novel characteristics of the claimed composition, method or structure.

[0490] As used herein, the singular form “a”, “an” and “the” include plural references unless the context clearly dictates otherwise. For example, the term “a unit” or “at least one unit” may include a plurality of units, including combinations thereof.

[0491] The words “example” and “exemplary” are used herein to mean “serving as an example, instance or illustration”. Any embodiment described as an “example or “exemplary” is not necessarily to be construed as preferred or advantageous over other embodiments and/or to exclude the incorporation of features from other embodiments.

[0492] The word “optionally” is used herein to mean “is provided in some embodiments and not provided in other embodiments”. Any particular embodiment of the invention may include a plurality of “optional” features unless such features conflict.

[0493] Throughout this application, various embodiments of this invention may be presented in a range format. It should be understood that the description in range format is merely for convenience and brevity and should not be construed as an inflexible limitation on the scope of the invention. Accordingly, the description of a range should be considered to have specifically disclosed all the possible sub-ranges as well as individual numerical values within that range. For example, description of a range such as from 1 to 6 should be considered to have specifically disclosed sub-ranges such as from 1 to 3, from 1 to 4, from 1 to 5, from 2 to 4, from 2 to 6, from 3 to 6 etc., as well as individual numbers within that range, for example, 1, 2, 3, 4, 5, and 6. This applies regardless of the breadth of the range.

[0494] Whenever a numerical range is indicated herein (for example “10-15”, “10 to 15”, or any pair of numbers linked by these another such range indication), it is meant to include any number (fractional or integral) within the indicated range limits, including the range limits, unless the context clearly dictates otherwise. The phrases “range/ranging/ranges between” a first indicate number and a second indicate number and “range/ranging/ranges from” a first indicate number “to”, “up to”, “until” or “through” (or another such range-indicating term) a second indicate number are used herein interchangeably and are meant to include the first and second indicated numbers and all the fractional and integral numbers therebetween.

[0495] Unless otherwise indicated, numbers used herein and any number ranges based thereon are approximations within the accuracy of reasonable measurement and rounding errors as understood by persons skilled in the art

[0496] It is appreciated that certain features of the invention, which are, for clarity, described in the context of separate embodiments, may also be provided in combination in a single embodiment. Conversely, various features of the invention, which are, for brevity, described in the context of a single embodiment, may also be provided separately or in any suitable sub-combination or as suitable in any other described embodiment of the invention. Certain features described in the context of various embodiments are not to be considered essential features of those embodiments, unless the embodiment is inoperative without those elements.

[0497] Although the invention has been described in conjunction with specific embodiments thereof, it is evident that many alternatives, modifications and variations will be apparent to those skilled in the art. Accordingly, it is intended to embrace all such alternatives, modifications and variations that fall within the spirit and broad scope of the appended claims. All publications, patents and patent applications mentioned in this specification are herein incorporated in their entirety by reference into the specification, to the same extent as if each individual publication, patent or patent application was specifically and individually indicated to be incorporated herein by reference. In addition, citation or identification of any reference in this application shall not be construed as an admission that such reference is available as prior art to the present invention.

[0498] All publications, patents and patent applications mentioned in this specification are herein incorporated in their entirety by reference into the specification, to the same extent as if each individual publication, patent or patent application was specifically and individually indicated to be incorporated herein by reference. In addition, citation or identification of any reference in this application shall not be construed as an admission that such reference is available as prior art to the present invention. To the extent that section headings are used, they should not be construed as necessarily limiting. In addition, any priority document(s) of this application is/are hereby incorporated herein by reference in its/their entirety.

LIST OF REFERENCE SIGNS

[0499]

TABLE-US-00001 energy storage (TES) system 100 chiller 102/150 fluid distribution system 104 controller 105 pumps 106 flow control mechanisms 107 piping 108 to 108T monitoring components 109 array 110 ice bricks 112, 112B, 112C, 112D ice capsules 114, 114C, 114Cy first fluid 120 second fluid 122 third fluid 124 air 126 cooling load 130 air compressor 140 Heat exchanger (HE) 142, 152, 170 filling nozzle 202 narrow-side spacers 204 broad-side spacers 206 rectangular enclosure 220 Mounting brackets 222 inlet/outlet pipes 224 end panels 226 support panels 227 interconnecting piping 228 base frame 232 ridge 250, 252 lower part 254 upper part 256 protrusions 260 general flow direction 290 meander pattern 291 discharging process 500 subsets 520, 520A, 520B 520, 520A, 520B spacers 600, 620 flaps 602 protrusions 603 vertical bars 621 horizontal bars 622 gaps 624 flow area 630 curved arrows 640 flows 650 tube 712 overall cross-section of the tube 712A front end element 713A back end element 713B inlet 714A outlet 714B capsule 715 spaces 716 stacks of capsules 717 flow paths 718 free flow cross-sectional area in the liquid 718A state of the second fluid free flow cross-sectional area in the frozen 718B state of the second fluid