Flammable Gas Concentration Reducer and Inert Gas Generator

Abstract

A remediation method and device for combustible gas in a room is disclosed. An inlet and outlet opening between ambient room air and the interior of a device are used with a sensor. Flame arrestor quench screens are used to control a fire within a chamber having an impeller causing air flow. A pilot flame situated within the combustion chamber burns combustible gas while temperature, pressure, and oxygen sensor devices are used to modify air flow as necessary for optimum combustion within the device.

Claims

1. A method of leak detection and/or remediation of combustible gas in a room, comprising the steps of: maintaining a first flow rate of ambient air from said room into an interior of a device; maintaining a pilot flame within said interior of said device; detecting a rise in temperature as a result of said pilot flame increasing in size due to combustion of gases in said ambient air; based on said detecting, increasing said flow rate to a second rate above said first flow rate; burning said combustible gas within said interior of said device; exhausting a resultant gaseous product.

2. The method of claim 1, wherein said exhausting is to said room by way of a filter which is part of a central air system for a building which comprises said room.

3. The method of claim 1, further comprising a step, while carrying out said step of burning, of detecting oxygen levels within said interior of said device. and adjusting flow rate to provide oxygen levels between a desired threshold for optimal combustion within said interior of said device.

4. The method of claim 1, further comprising detecting a rise in pressure and oxygen concentration of air passing through said device and lowering said flow rate based on a rise in pressure.

5. The method of claim 1, wherein at least some of said gas is rendered inert by a catalytic converter simultaneous to said burning.

6. The method of claim 1, wherein after said second flow rate is carried out for a pre-determined period of time and said temperature remains above a pre-determined amount within said device a further step of introducing water into said device is carried out.

7. A device for remediation of gases in a room, comprising: an inlet open to ambient air within a room and a first interior space of said device with at least one sensor; an outlet open to outside of said device; a first flame arrestor quench screen situated between said first interior space and an impeller and a second flame arrestor quench screen between a combustion chamber and said outlet, said impeller causing air flow in a direction from said inlet to said outlet; a pilot flame situated within said combustion chamber.

8. The device of claim 7, wherein said outlet is open to said ambient air within said room.

9. The device of claim 7, wherein said at least one sensor comprising at least two of a pressure sensor, temperature sensor, and oxygen concentration sensor.

10. The device of claim 9, wherein a catalytic converter is situated downstream from said impeller.

11. The device of claim 10, wherein a pressure release valve is situated downstream from said impeller.

12. The device of claim 9, wherein upon detection of one of an increase in pressure, an increase in temperature, or a decrease in oxygen concentration by a respective at least one sensor, a rotation rate of said impeller is increased.

13. The device of claim 9, further comprising a water inlet which is opened upon detection of a temperature above a pre-defined threshold for a pre-defined period of time, wherein said detection is based on output from said temperature sensor.

14. A kit comprising the device of claim 8 and a central air system of a building in which said device is situated, wherein said central air system comprises a filter through which air from said central air system passes and, in addition, air from said outlet passes before reaching said room.

15. The kit of claim 14, wherein ducts extend from said central air system to said room and said output of said device connects to said ducts.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0019] FIG. 1 is a diagram of a remediation device used to carry out embodiments of the disclosed technology.

[0020] FIG. 2 is a high level block diagram of methods of carrying out embodiments of the disclosed technology.

[0021] FIG. 3 is a further block diagram of aspects of the disclosed technology.

[0022] FIG. 4 is a high level block diagram of devices which can be used to aid in carrying out aspects of the disclosed technology.

DETAILED DESCRIPTION OF EMBODIMENTS OF THE DISCLOSED TECHNOLOGY

[0023] A leak detection and remediation method and device for combustible gas in a room is disclosed. An inlet and outlet opening between ambient room air and the interior of a device are used with several sensors. Flame arrestor quench screens are used to control a fire within a chamber having an impeller causing air flow. A pilot flame situated within the combustion chamber burns combustible gas while temperature, pressure, and oxygen sensor devices are used to modify air flow as necessary for optimum combustion within the device.

[0024] Embodiments of the technology will become clearer in view of the following description of the figures.

[0025] FIG. 1 is a diagram of a remediation device used to carry out embodiments of the disclosed technology. The remediation device provides carbon monoxide, natural gas and other flammable gas concentration reduction to the interior of living and work spaces, such as a room, as defined in the Summary of the Disclosed Technology. The device has an air inlet opening 11 which receives air from a room, the room being protected by this device from combustible gases. The outlet 502, which can be on a different, opposite, or same side as the inlet 11 vents gas out of the device back into the room or a space exterior to the room (such as the outside atmosphere of the earth, unconstrained or contained by any man-made structure). A power source and controller supply electricity along data bus 22. Devices which can be used in connection with operation of the data bus 22 and a hardware controller are shown and described with reference to FIG. 4. A circulation fan 48 to safely disperse the heat of combustion is also employed in embodiments of the disclosed technology.

[0026] Air from a room and/or from outside the remediation device is drawn into the inlet 11 in Zone 1 by the suction produced by impeller 31. In Zone 1, the temperature of the gas is approximately equal to that in the living space, but the pressure is reduced due to the suction. The gas passes through a flame arrestor quench screen 13 before passing through a housing 21 which can be insulated from fire (non-flammable) and blast resistant. The air then enters into Zone 2 (the arrows in outline indicate direction of flow). A reusable pressure relief valve and outlet system 201 are used in embodiments of the disclosed technology to prevent pressure inside the device from becoming too high.

[0027] In Zone 2, the pressure remains reduced due to the suction. The gas is analyzed for temperature using a temperature sensing device (thermocouple) 26, pressure using a pressure sensing device (piezoelectric pressure transducer) 27, and oxygen concentration using an oxygen concentration measurement device 28 before passing through another flame arrestor quench screen 29 to Zone 3.

[0028] Zone 3 begins with variable-speed electric impeller 31 that draws in the gas. In Zone 3, downstream of impeller 31, the pressure and temperature are greater than the room pressure and temperature respectively in embodiments of the disclosed technology. Temperature sensors 32 and pressure sensors 33 monitor the unburned gas. Some of the gas, in embodiments of the disclosed technology, proceeds to an electrically heated catalytic converter 35, while the remainder, such as is sufficient for wall-cooling, proceeds through a bypass 36. In the event of excessive pressure build up in Zone 3, reusable pressure relief valve and outlet system 37 vents excess gas outside the system. The gases recombine in Zone 4.

[0029] Zone 4 comprises or contains the partially combusted gases so the gas temperature is the hottest in the system and is typically greater than 100 C. to avoid water condensation. Temperature, pressure and oxygen content are monitored by respective sensors 41, 42 and 43 respectively. Pressure in Zones 3 and 4 are controlled by balancing the gas inflow driven by impeller 31 and electrically-controlled throttle valve 45. In the event of excessive pressure build up in Zone 4, reusable pressure relief valve and outlet system 44 vents excess gas outside the system. The gas then passes through flame arrestor quench screen 46 to Zone 5.

[0030] The gas, now comprises nitrogen and a higher than atmospheric and/or room level of carbon dioxide, as well as a lower than atmospheric and/or room level of oxygen passes out of the remediation device through flame arrestor quench screen 501 and through outlet 502 back to the room or to the outside.

[0031] FIG. 2 is a high level block diagram of methods of carrying out embodiments of the disclosed technology. The flow chart also shows the location in which the steps take place and/or items which are acted upon. Inside room 100, remediation device 200 is placed (or, at least an intake vent, inlet or opening of a remediation device being there-in the room). Ambient air 110 from within the room 100 is sucked by an impeller/fan, which exists in the remediation device (see FIG. 1), into the device at a first flow rate 210. A pilot flame 220 is maintained at a first minimal amount. A pilot flame for purposes of this disclosure is defined as a flame which is kept alight even when no combustible gas in the room is detected and uses no more than 500 watts. When the pilot flame is methane fed, the methane flow rate will have a maximum burn rate of 1.9 standard cubic feet per hour. Pilot flames can be fed by the same natural gas that supplies a structure where the device is being used. When using oil heat, the oil for the furnace can be used to fuel the pilot flame. In all houses, offices, etc., not just those electrically heated, an electric powered catalytic wire mesh or catalytic converter serves the same purpose as a pilot flame. Thus, when pilot flame is claimed, unless specified as the burning of fossil fuels or another solid or liquid, the term includes an electric powered catalytic wire mesh or catalytic converter.

[0032] A temperature sensor (e.g. thermometer) is used in step 230 to determine if there is a temperature rise inside, on the inner surface of, or the outer surface of the remediation device 200. In other embodiments, the temperature is measured within the room, being the ambient room temperature. When the temperature rises above a pre-defined threshold, such as above 100, 120, or 150 degrees Celsius when measuring areas outside of the Zone where the pilot flame is located. In other embodiments, the temperature threshold rise is defined based on a baseline temperature measured near the pilot flame, such as a thermometer in the same Zone. In such a case, the temperature rise in step 230 is 10 degrees, 20 degrees, or 40 degrees Celsius over the baseline set by the pilot flame alone. The temperature rise in any of these embodiments is due to an increase in heat release as the pilot flame increases in size due to the incineration of combustible gases entering into the remediation device. If no temperature rise happens, then step 210 and 220 are repeated cyclically until this situation changes and the temperature rises in step 230.

[0033] Once the temperature rise is detected, the rise being above any of the thresholds defined in the previous paragraph, the flow rate of air into the remediation device is increased in step 240. This is in order to increase the rate at which the gas is combusted, and create a safe atmosphere of the ambient air 110 in the room 100. For example, the first flow rate can be 25 standard cubic feet per minute (SCFM) for a room with 1000 cubic feet (or within 10% of this size). The increased flow rate can be 250 SCFM. A 24 square inch opening (such as 212 rectangular gas inlet opening or 2.75 radius circular inlet) provides adequate gas sampling with minimal noise at the low flow rate and satisfactory performance even for higher flow rates. The maximum heat release in the event of a methane leak occurs if the mixture is 9.5% methane and 90.5% air (19% O2 and 71.5% of N2 and trace gases). Combusting 250 SCFM results in a lower heating rate (based on the lower heating value) of 380 Kilowatts.

[0034] In step 250, gas is burned within the device, referring to combustible gas beyond that which is supplied to support the pilot flame. This is described further with reference to FIG. 1. One can also, in embodiments of the disclosed technology, employ a catalytic converter in step 250 to render some of the gas inert without resorting to burning all of the gas. Then the gaseous product is exhausted in step 260 out of the device 200. The gaseous product is no longer or less combustible and is vented either back into the room in step 262 or to the outside in step 264. When the gas is exhausted back into the room, it can be through a filter present in the room for an air flow system which is part of the building. For example, air conditioning and heating units (whether standalone or a central air system) typically use filters. When the device of embodiments of the disclosed technology exhausts air from the device, it does so through such a filter before the air is sent back into the room.

[0035] For purposes of this disclosure, central air is defined as devices and methods of structural cooling of a building (or, at least, multiple rooms) in which a centralized unit cools or heats air before circulating it throughout the multiple rooms or building. This is in direct contrast with systems that rely on individual units in an individual room. The air which is heated or cooled by a central air system is usually transported to various rooms by duct work.

[0036] FIG. 3 is a further block diagram of aspects of the disclosed technology. Step 240 of increasing the flow rate of air from FIG. 2 is shown again. This causes the device to burn (more) gas within the device in step 250. However, other factors, in embodiments of the disclosed technology, can be taken into account to adjust the flow rate. For example, in step 270 it is determined whether the oxygen levels are out of bounds. That is, combustion requires oxygen. If the oxygen levels are too low, combustion will decrease or stop. If the oxygen levels are too high, combustion will be too rapid, leading to dangerous heat release rates and steep rises in temperature and pressure. Thus, the flow rate is increased or decreased accordingly in step 255, bringing in ambient air at a greater or lesser rate to increase or decrease the amount of oxygen within the remediation device compared to the amount of other gases. This can be determined, in part, by oxygen sensors placed within and outside of (in the room) the remediation device.

[0037] Further, if the pressure is above a pre-defined threshold in step 272, the flow rate of the air into the remediation device 200 can be adjusted. Pressure too high is dangerous and can cause malfunction or explosions. Therefore, pressure overrides oxygen level bounds (e.g. step 272 overrides step 270), and can cause a lowering of the air flow rate in step 255 to decrease the rate of combustion. When the pressure is back to safe levels or further below same, the air flow rate can again be increased.

[0038] Still further, it is desired in some embodiments of the disclosed technology to ensure that combustion lasts only for a certain amount of time such as 10 minutes, 15 minutes, 30 minutes, 60 minutes, or 6 hours. Allowing combustion to proceed longer might be the result of unsafe conditions for which operation of the device and the flame associated therewith will only produce more danger when the goal of the device is to reduce danger. Thus, in a situation where one must remediate for too long a period of time or at too high of temperatures or at too high of pressures (for a period of time) can be dangerous. When such conditions are reached, then water is inputted into the device 200 in step 280 from a water source 290. The pilot light is obviously also shut off and gas supply is reduced to zero. In this manner, the device stops functioning as a safety precaution. Pressure release or the ceasing of the pilot light takes place, in embodiments, at 75 psig or less. The temperature of a methane-air flame can exceeds 3500 F., but sufficient cooling will insure no other part of the device exceeds 1800 F. In the embodiment using a catalytic converter, operating temperatures range from 400 to 1800 F. Those portions of the device expected to be exposed to elevated temperatures are manufactured of materials capable of withstanding such heat. Similarly, those portions of the device expected to be exposed to elevated pressures are manufactured of materials capable of withstanding such forces.

[0039] FIG. 4 is a high level block diagram of devices which can be used to aid in carrying out aspects of the disclosed technology. Device 600 comprises a processor 650 that controls the overall operation of the computer by executing the device's program instructions which define such operations. The device's program instructions may be stored in a storage device 620 (e.g., magnetic disk, database) and loaded into memory 630 when execution of the console's program instructions is desired. Thus, the device's operation will be defined by the device's program instructions stored in memory 630 and/or storage 620, and the console will be controlled by processor 650 executing the console's program instructions. A device 600 also includes one or a plurality of input network interfaces for communicating with other devices via a network (e.g., the internet). The device 600 further includes an electrical input interface. A device 600 also includes one or more output network interfaces 610 for communicating with other devices. Device 600 also includes input/output 640 representing devices which allow for user interaction with a computer (e.g., display, keyboard, mouse, speakers, buttons, etc.). One skilled in the art will recognize that an implementation of an actual device will contain other components as well, and that FIG. 4 is a high level representation of some of the components of such a device for illustrative purposes. It should also be understood by one skilled in the art that the method and devices depicted in FIGS. 1 through 3 may be implemented on a device such as is shown in FIG. 4.

[0040] While the disclosed technology has been taught with specific reference to the above embodiments, a person having ordinary skill in the art will recognize that changes can be made in form and detail without departing from the spirit and the scope of the disclosed technology. The described embodiments are to be considered in all respects only as illustrative and not restrictive. All changes that come within the meaning and range of equivalency of the claims are to be embraced within their scope. Combinations of any of the methods, systems, and devices described hereinabove are also contemplated and within the scope of the invention.