MATERIAL COOLING SYSTEM HAVING A VARIABLE HEAT REJECTION INTERFACE
20230384011 · 2023-11-30
Inventors
Cpc classification
F25B2700/2106
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B39/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B49/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B41/20
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F25B49/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B39/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B41/20
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
A cooling system for an industrial facility includes a facility that has a thermal energy output and an input, a dry cooler that includes a plurality of blowers, an evaporative cooling tower, a fluid-cooled chiller, a valving system that receives a thermally-charged media from the thermal energy output for delivery to at least one of the dry cooler, the evaporative cooling tower, and the fluid-cooled chiller, and a temperature sensor that is in communication with the valving system via a controller. The temperature sensor measures a current ambient temperature and cooperates with the controller to automatically adjust the valving system to direct the thermally-charged media to one of the dry cooler, the evaporative cooling tower, and the fluid-cooled chiller for rejecting heat from the thermally-charged media to define a thermally-receptive media. The cooling system further includes a return conduit that delivers the thermally-receptive media to the input.
Claims
1. A cooling system for an industrial facility, the cooling system comprising: a facility having a thermal energy output and an input; a dry cooler that includes a plurality of blowers; an evaporative cooling tower; a fluid-cooled chiller; a valving system that receives a thermally-charged media from the thermal energy output for delivery to at least one of the dry cooler, the evaporative cooling tower, and the fluid-cooled chiller; a temperature sensor in communication with the valving system via a controller, wherein the temperature sensor measures a current ambient temperature and cooperates with the controller to automatically adjust the valving system to direct the thermally-charged media to one of the dry cooler, the evaporative cooling tower, and the fluid-cooled chiller for rejecting heat from the thermally-charged media to define a thermally-receptive media; and a return conduit that delivers the thermally-receptive media to the input.
2. The cooling system of claim 1, wherein the valving system operates to deliver the thermally-charged media to the fluid-cooled chiller when the ambient temperature is within a predetermined temperature range.
3. The cooling system of claim 2, wherein the valving system operates to deliver the thermally-charged media to the dry cooler when the ambient temperature is below the predetermined temperature range.
4. The cooling system of claim 3, wherein the valving system operates to deliver the thermally-charged media to the evaporative cooling tower when the ambient temperature is above the predetermined temperature range.
5. The cooling system of claim 4, wherein the predetermined temperature range is between approximately 30 degrees Fahrenheit at dry bulb and approximately 70 degrees Fahrenheit at dry bulb.
6. The cooling system of claim 1, wherein the controller is incorporated within the valving system.
7. The cooling system of claim 1, wherein the valving system, the dry cooler, the evaporative cooling tower, and the fluid-cooled chiller are incorporated within a self-contained assembly.
8. The cooling system of claim 1, wherein the thermally-charged media is delivered from the thermal energy output to the valving system via a gravity-operated drain.
9. The cooling system of claim 1, wherein the return conduit includes a process pump that directs the thermally-receptive media to the input.
10. The cooling system of claim 1, further comprising a filtration system that is positions between the thermal energy output and the valving system.
11. The cooling system of claim 1, further comprising a supplemental delivery conduit having a cooling fluid that extends from the fluid-cooled chiller to the dry cooler and the evaporative cooling tower.
12. The cooling system of claim 11, wherein the dry cooler and the evaporative cooling tower provide a supplemental thermal exchange system that supports the fluid-cooled chiller.
13. A cooling system for an industrial facility, the cooling system comprising: a dry cooler that includes a plurality of blowers; an evaporative cooling tower; a fluid-cooled chiller; a valving system that delivers a thermally-charged media to one of the dry cooler, the evaporative cooling tower, and the fluid-cooled chiller, wherein the valving system is configured to receive the thermally-charged media from an injection molding facility; a temperature sensor in communication with the valving system via a controller, wherein the temperature sensor measures a current ambient temperature and cooperates with the controller to automatically adjust the valving system to direct the thermally-charged media to one of the dry cooler, the evaporative cooling tower, and the fluid-cooled chiller for rejecting heat from the thermally-charged media to define a thermally-receptive media; and a supplemental cooling system that extends between the fluid-cooled chiller to the dry cooler and between the fluid-cooled chiller to the evaporative cooling tower, the supplemental cooling system assisting the fluid-cooled chiller in rejecting heat from the thermally-charged media.
14. The cooling system of claim 13, wherein: the valving system operates to deliver the thermally-charged media to the fluid-cooled chiller when the current ambient temperature is within a predetermined temperature range; the valving system operates to deliver the thermally-charged media to the dry cooler when the current ambient temperature is below the predetermined temperature range; and the valving system operates to deliver the thermally-charged media to the evaporative cooling tower when the current ambient temperature is above the predetermined temperature range.
15. The cooling system of claim 14, wherein the predetermined temperature range is between approximately 30 degrees Fahrenheit at dry bulb and approximately 70 degrees Fahrenheit at dry bulb.
16. The cooling system of claim 13, wherein the valving system, the dry cooler, the evaporative cooling tower, and the fluid-cooled chiller are incorporated within a self-contained assembly.
17. The cooling system of claim 13, wherein a filtration system is positioned upstream of the valving system.
18. The cooling system of claim 13, wherein the controller is incorporated within the valving system.
19. A method for operating a cooling system for a facility, the method including steps of: delivering a thermally-charged media from a facility to a cooling system; measuring a temperature of ambient air surrounding the facility utilizing a temperature sensor; operating a valving system based upon the temperature of the ambient air to deliver the thermally-charged media to one of a dry cooler, an evaporative cooling tower and a fluid-cooled chiller; rejecting heat from the thermally-charged media to define a thermally-receptive media; and returning the thermally-receptive media to the facility.
20. The method of claim 19, wherein the step of operating the valving system includes: operating the valving system to deliver the thermally-charged media to the fluid-cooled chiller when the temperature of the ambient air is within a predetermined temperature range; operating the valving system to deliver the thermally-charged media to the dry cooler when the temperature of the ambient air is below the predetermined temperature range; and operating the valving system to deliver the thermally-charged media to the evaporative cooling tower when the temperature of the ambient air is above the predetermined temperature range.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0008] In the drawings:
[0009]
[0010]
[0011]
[0012]
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0013] As exemplified in
[0014] Referring again to
[0015] Referring again to
[0016] Similarly, when the ambient temperature 52 is within the predetermined temperature range, use of the fluid-cooled chiller 42 maintains the fluid within a particular cooling chamber 60. The thermally-charged media 46 is moved through this cooling chamber 60 of the fluid-cooled chiller 42. In this manner, heat 16 can be extracted from the thermally-charged media 46 to a separate media within the cooling chamber 60 of the fluid-cooled chiller 42. Accordingly, each of the fluid-cooled chiller 42 and the dry cooler 36 operate in a manner that minimizes or eliminates the possibility of freezing or icing during operation of the cooling system 10.
[0017] Referring again to
[0018] Referring again to
[0019] According to the various aspects of the device, these cooling components 54 of the cooling system 10 can be separate components that are separated from one another. In such an aspect of the device, these cooling components 54 can be connected by various material delivery conduits 56 and other similar connections for delivering the thermally-charged media 46 from the facility 12, through one or more components of the cooling system 10, and then back to the facility 12 or to a separate location. It is also contemplated that two or all of the cooling components 54 of the cooling system 10 can be incorporated into a single self-contained assembly that is built within a single structure. This single structure can be manufactured on site, can be manufactured off site or a combination thereof. In such an aspect of the device, the dry cooler 36, the evaporative cooling tower 40 and the fluid-cooled chiller 42 can be manufactured as a unit or integral assembly. Accordingly, the movement of the thermally-charged media 46 can be performed efficiently and within a relatively small area.
[0020] According to various aspects of the device, the predetermined temperature range for the cooling system 10 can be between approximately 30° F. and 69° F. These temperatures are typically monitored in a dry bulb setting where the temperature sensor 48 is within the ambient atmosphere or sheltered from precipitation and solar energy. It is contemplated that this predetermined temperature range can vary depending on the elevation and climate in which the facility 12 is located, the design of the facility 12, the thermal exchange requirements and other factors. Accordingly, the predetermined temperature range noted above is an exemplary range of temperatures and is provided as a non-limiting example.
[0021] Referring now to
[0022] According to
[0023] When the cooling fluid 110 from the fluid-cooled chiller 42 is delivered to the evaporative cooling tower 40 or the dry cooler 36, the heat 16 delivered by the cooling fluid 110 is rejected into atmosphere or rejected into a separate thermal exchange media 14 for recycling or reuse of the captured heat 16. The cooling fluid 110, which is now at a lower temperature, is returned to the condenser 96 of the fluid-cooled chiller 42 to again receive the rejected heat 16 from the thermally-charged media 46. After leaving the chiller, the now-spent thermally-charged media 46 is converted to thermally-receptive media 114 and is returned to the facility 12 via a fluid pump 116 and the input 34.
[0024] Referring again to
[0025] As is exemplified in
[0026] As exemplified in
[0027] According to various aspects of the device, the various fluids and fluid media of the cooling system 10 are operated utilizing one or more fluid pumps 116. It is contemplated that each of these fluid pumps 116 includes a primary pump 140 and a secondary pump 142 that operate in combination to ensure continuous operation of the cooling system 10. In each of the fluid pump locations, the primary pump 140 and secondary pump 142 are switched periodically, such as weekly, to ensure proper operation of each of the primary pump 140 and the secondary pump 142. This switching of operation between the primary pump 140 and secondary pump 142 ensures that the fluid pumps 116 are not idle for an extended period of time. This also assists in maintaining and extending the life of the fluid pumps 116 of the cooling system 10. The use of the primary pump 140 and the secondary pump 142 also allows for periodic maintenance of either the primary pump 140 or the secondary pump 142 without causing a shutdown of the entire system.
[0028] According to the various aspects of the device, the various cooling components 54 of the cooling system 10 operate cooperatively to efficiently reject heat 16 from a thermally-charged media 46. As described herein, the rejection of heat 16 by the fluid-cooled chiller 42 typically includes either the evaporative cooling tower 40 or the dry cooler 36, depending upon the ambient temperature 52, to complete rejection of heat 16 from the thermally-charged media 46. These processes serve to convert the thermally-charged media 46 that is delivered from the facility 12 to the thermally-receptive media 114 that is delivered back to the facility 12 for continuing the thermal rejection process.
[0029] Referring now to
[0030] As described herein, the valving system 44 utilizes a controller 50 and cooperates with the controller 50 to operate the various control valves 80 of the valving system 44. It is contemplated that the controller 50 can be incorporated within the one or more control valves 80 of the valving system 44. It is also contemplated that the cooling system 10 can include a central controller 50 that operates the various control valves 80 of the valving system 44 as well as the motors, blowers 38 and fluid pumps 116 of the dry cooler 36, the evaporative cooling tower 40 and the fluid-cooled chiller 42.
[0031] These cooling components 54 can be sized and configured based upon the amount of heat 16 being rejected from a particular facility 12. By way of example, and not limitation, the dry cooler 36 can include one or more blowers 38. Typically, the dry cooler 36 includes a plurality of blowers 38 that can be used for moving a media, typically ambient air, across flow conduits 90 containing the thermally-charged media 46. These blowers 38 operate to reject heat 16 from the thermally-charged media 46 to atmosphere. Additionally, the evaporative cooling tower 40 can be sized to accommodate a particular cooling capacity. The number of evaporative cooling towers 40 can also be adjusted depending on the heat-rejecting needs of the facility 12. Additionally, the fluid-cooled chiller 42 can include a single chiller or multiple chillers that can operate in combination.
TABLE-US-00001 Degrees F. Degrees F. Chillers Electrical Usage Measures at HRS/ Measured @ Cond. KW Hrs EQUIPMENT OPERATING Wet Bulb YEAR Dry Bulb Temp. (540 Ton) *cooling tower WATER 65 0 100/104 72 0.46 A - for chiller condensers water evaporated 62 18 95/99 68 0.407 1% flow 61 129 90/94 68 0.407 1,756 total operating hr/yr 540 ton @ 3 gal/ton × 1% = 16.2 gpm 60 252 85/89 67 0.407 16.2 gpm × 1756 hr/yr × 60 58 347 80/84 65 0.407 56 444 75/79 63 0.407 1,706,832 gallons/year 54 566 70/74 61 0.407 540 ton × 1756 hrs/yr × .427 kw hr = 404,898 kw/yr 52 634 65/69 * dry cooler 49 619 60/64 B - for chiller condensers 0 46 601 55/59 water evaporated 43 672 50/54 39 712 45/49 5,680 total operating hours per year 36 777 40/44 32 849 35/39 29 816 * 30/34.sup. 24 601 25/29 C - dry cooler to supply chilled water (water cooled chiller off) 20 385 20/24 0 16 201 15/19 water evaporated 11 82 10/14 6 36 5/9 1,321 total operating hours per year 2 11 0/4 −3 3 −5/−1 −8 1 −10/−6 −13 1 −15/−11 Total Hours= 8757 Total water evaporated = 1,706,832 gallon/year
[0032] Referring again to
[0033] Referring again to
[0034] The dry cooler 36 is utilized when the ambient temperature 52 is below the predetermined temperature range. Typically, in this condition, it may not be necessary for the fluid-cooled chiller 42 to operate in these lower temperatures. Accordingly, the cooled-ambient air may be sufficient for extracting or rejecting heat 16 from the thermally-charged media 46 for creating the thermally-receptive media 114 that is returned to the facility 12.
[0035] It is contemplated that in conditions where the evaporative cooling tower 40 and/or the dry cooler 36 are supplementing the fluid-cooled chiller 42 for rejecting heat 16 that most electricity will be utilized during use of the cooling system 10. Because the dry cooler 36 operates in the lowest temperature ranges, this aspect of the device may utilize the least amount of electricity as the other components of the cooling system 10 may not be needed for rejecting heat 16 from the thermally-charged media 46. Again, the amount of electricity used can vary depending upon certain atmospheric and environmental conditions that can bear on humidity levels, temperature and other environmental factors that relate to the location where the facility 12 is located.
[0036] With respect to the exemplary device described above, the annual electrical load drawn by the cooling system 10 can be within a range of approximately 1.5 million kilowatts per year to 2.25 million kilowatts per year.
[0037] Utilizing the cooling system 10, a facility 12 can operate various processes and reject heat 16 generated through these processes at any time of year regardless of the ambient temperature 52 and other environmental conditions and factors. These environmental factors and conditions can include, but are not limited to, geographic location, climate, altitude, humidity, barometric pressure and other environmental conditions. Accordingly, use of fluid, typically water, can be maximized for use at certain times of the year and under certain particular conditions depending on the cost and availability of water. It is contemplated that where water is scarce, such as during a drought or where most water is frozen, the fluid-cooled chiller 42 and the dry cooler 36 can operate in combination to achieve at least a portion of the thermal exchange function for the cooling system 10.
[0038] It is to be understood that variations and modifications can be made on the aforementioned structure without departing from the concepts of the present invention, and further it is to be understood that such concepts are intended to be covered by the following claims unless these claims by their language expressly state otherwise.