US20080112869A1 - Direct contact liquid air contaminant control system - Google Patents
Direct contact liquid air contaminant control system Download PDFInfo
- Publication number
- US20080112869A1 US20080112869A1 US11/741,686 US74168607A US2008112869A1 US 20080112869 A1 US20080112869 A1 US 20080112869A1 US 74168607 A US74168607 A US 74168607A US 2008112869 A1 US2008112869 A1 US 2008112869A1
- Authority
- US
- United States
- Prior art keywords
- scrubber
- liquid absorbent
- carbon dioxide
- air
- rotor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0454—Controlling adsorption
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/1412—Controlling the absorption process
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/1456—Removing acid components
- B01D53/1475—Removing carbon dioxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/18—Absorbing units; Liquid distributors therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/75—Multi-step processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
- B63G—OFFENSIVE OR DEFENSIVE ARRANGEMENTS ON VESSELS; MINE-LAYING; MINE-SWEEPING; SUBMARINES; AIRCRAFT CARRIERS
- B63G8/00—Underwater vessels, e.g. submarines; Equipment specially adapted therefor
- B63G8/36—Adaptations of ventilation, e.g. schnorkels, cooling, heating, or air-conditioning
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B64—AIRCRAFT; AVIATION; COSMONAUTICS
- B64D—EQUIPMENT FOR FITTING IN OR TO AIRCRAFT; FLIGHT SUITS; PARACHUTES; ARRANGEMENTS OR MOUNTING OF POWER PLANTS OR PROPULSION TRANSMISSIONS IN AIRCRAFT
- B64D13/00—Arrangements or adaptations of air-treatment apparatus for aircraft crew or passengers, or freight space, or structural parts of the aircraft
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/50—Carbon oxides
- B01D2257/504—Carbon dioxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/45—Gas separation or purification devices adapted for specific applications
- B01D2259/4566—Gas separation or purification devices adapted for specific applications for use in transportation means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/45—Gas separation or purification devices adapted for specific applications
- B01D2259/4566—Gas separation or purification devices adapted for specific applications for use in transportation means
- B01D2259/4575—Gas separation or purification devices adapted for specific applications for use in transportation means in aeroplanes or space ships
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B64—AIRCRAFT; AVIATION; COSMONAUTICS
- B64D—EQUIPMENT FOR FITTING IN OR TO AIRCRAFT; FLIGHT SUITS; PARACHUTES; ARRANGEMENTS OR MOUNTING OF POWER PLANTS OR PROPULSION TRANSMISSIONS IN AIRCRAFT
- B64D13/00—Arrangements or adaptations of air-treatment apparatus for aircraft crew or passengers, or freight space, or structural parts of the aircraft
- B64D13/06—Arrangements or adaptations of air-treatment apparatus for aircraft crew or passengers, or freight space, or structural parts of the aircraft the air being conditioned
- B64D2013/0603—Environmental Control Systems
- B64D2013/0651—Environmental Control Systems comprising filters, e.g. dust filters
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T50/00—Aeronautics or air transport
- Y02T50/50—On board measures aiming to increase energy efficiency
Definitions
- the present invention generally relates to an air environment control system (ECS) that revitalizes air and more specifically to the apparatus and methods that control humidity and temperature of cabin air of aircraft and spacecraft while removing carbon dioxide and other trace gas contaminates.
- ECS air environment control system
- Liquid amine (methanol amine water solutions) based carbon dioxide and trace gas contaminant removal apparatus and processes for regeneration of air have been used in nuclear submarines for over forty years. Such systems are used to remove carbon dioxide for the breathing air and depend on gravity to process the liquid carbon amine or other liquids and air mixture.
- Centrifugal liquid and gas processors have been explored as described in the article “The Centrifugal Mass Exchange Apparatus in Air-Conditioning System of Isolated, Inhabited Object and Its Work Control”, by P. A. Barabash, et al, in Proceedings of the 4 th European Symposium on Space Environmental and Control Systems, Oct. 21-24, 1991.
- the article postulates use of a centrifugal apparatus to work with an air-conditioning system in a closed habitat system such as an orbital space station.
- a single stage system is proposed that keeps air temperature and humidity parameters within limits.
- the single stage rotor does not anticipate a more staged air process system using contaminant absorbent fluids and acid wash to provide carbon dioxide and other contaminant removal from a cabin air environment.
- present spacecraft and space stations typically employ apparatus dedicated exclusively to contaminant extraction from cabin air.
- Another apparatus is used for maintaining humidity and temperature of the cabin air.
- Each of these independent systems adds undesirable weight and consumes valuable space and power in a
- An improved environmental control system and method according to the present invention may comprise a carbon dioxide scrubber, a liquid absorbent stripper, a charcoal filter, and supporting containers, pumps and other elements.
- method for providing environmental control for cabin air of a vehicle comprises the steps of introducing a portion of the cabin air as air flow into a carbon dioxide scrubber and spraying a liquid mist into the air flow thereby modifying humidity, temperature and carbon dioxide concentration of the cabin air.
- an environmental control apparatus for cabin air of a vehicle comprises a contaminant scrubber wherein a contamination-control liquid is introduced as a mist into an air flow of a portion of the cabin air through the contaminant scrubber.
- the contamination-control liquid has a temperature lower than a temperature of the cabin air. Temperature of the cabin air is reduced and humidity of the cabin air is modified.
- an apparatus for controlling humidity and temperature of cabin air in a vehicle comprises a rotary contact processor for direct contact liquid absorbent and gas contaminant processing.
- FIG. 1 illustrates a functional block diagram of the invention
- FIG. 2 illustrates a functional block diagram of the major elements according to an embodiment of the invention
- FIG. 3 illustrates a functional cross-sectional view of a rotary liquid contact processor apparatus according to an embodiment of the invention.
- FIG. 4 is a flow chart of a method for providing environmental control for cabin air of a vehicle according to an embodiment of the invention.
- an environmental control system (ECS) 10 has an absorber element 20 and a stripper element 80 in fluid communication and in control/data communication.
- Support elements such as a control and data processor and an electric power source, not shown, are provided by existing platform equipment as is found on spacecraft and aircraft.
- the ECS 10 may be connected to the cabin air system of a vehicle to process the return air from use in a vehicle human environment, to decontaminate, cool and dehumidify the air, and to return cold clean air for use in a continuing cycle.
- the current system absorber element 20 uses a rotary process scrubber 30 and charcoal bed filter 26 to remove contaminants. Both liquid absorbent (such as an amine) and acid water are used in the scrubber 30 for direct contact liquid/vapor phase separation of contaminants.
- the stripper 80 may also use a rotary processor for liquid/vapor phase separation of liquid absorbent and carbon dioxide.
- the use of rotary processors allows operation in variable gravity environments such as experienced in aircraft and spacecraft and provides compact, light weight and reliable apparatus as compared to current art bulky, inefficient apparatus.
- the use of direct contact liquid/vapor processing allows more efficient heat transfer as compared to current technology, which relies on use of condensing heat exchangers, slurpers, and rotating centrifugal phase separators.
- a cold contamination-control liquid such as an acid water spray may be used in the air contaminant control system to remove absorbent vapor from the air and for temperature and humidity control.
- cabin air is introduced into the ECS 10 , and passes through the cold spray the air temperature may be reduced.
- the air may become saturated as it is cooled toward the temperature of the acid water and some of the moisture conveyed in the air may condense and mix with the acid water. Thus moisture content of the air may diminish. If the air does not become saturated with water as it is cooled to the temperature of the acid water spray, water may evaporate from the cold acid water spray and add the water content of the air. Additionally, cabin air may be cooled as it passes through the cold water spray.
- control of humidity may be the design limiting function of the system.
- the ECS 10 may be sized to process enough air to control the humidity. By doing so, the other functions, such as temperature control and contamination control, may be easily satisfied.
- Cabin air may be drawn through the scrubber 30 by a fan that may be used to aid vehicle cabin ventilation air flow.
- carbon dioxide and other contaminates may be removed from the air through direct contact with a cool liquid absorbent.
- the liquid absorbent removes carbon dioxide to form a carbonate complex.
- liquid absorbent as commonly understood in the art relates to carbon dioxide liquid absorbents, as for example, water solutions of methanol amine, ethanol amine, isopropyl amine, cesium carbonate, magnesium carbonate and similar solutions.
- the choice of liquid absorbent may be based on system operational factors such as carbon dioxide pressure, temperature, humidity, regeneration temperature and energy sources.
- the amines have a low vapor pressure at absorption conditions; however, without treatment some amine vapor may remain in the processed air to be introduced into the vehicle cabin as a contaminant.
- an acid water scrubber 60 may be included in the scrubber 30 to maintain amine pressure at acceptable levels, for example, about 1 ppm.
- the same process may absorb other basic trace gases such as ammonia.
- a mild acid, such as, citric, acetic, or hypo-phosphoric acid may reduce the amine vapor pressure to the desired levels.
- the acid water may serve as an anti-microbial with the potential for reducing bacterial contamination or spread of pathogens.
- the acid water solution may become very diluted, but the pH should be maintained relatively low, i.e., less than about 2 value. Additional acid may be added to the acid water scrubber 60 to maintain a low pH.
- acetic acid, vinegar may be produced onboard a vehicle using well known biological processes.
- the carbon dioxide scrubber 40 may act to absorb acidic trace gases.
- the combination of the carbon dioxide scrubber 40 and acid water scrubber 60 results in substantial removal of water soluble trace gases.
- These gases may be removed by a charcoal bed filter 26 downstream of the scrubber 30 .
- the charcoal bed filter 26 may be a single use or regenerable device depending on the mission requirements. Generally large portions of the trace contaminants are removed in the scrubber 30 thereby reducing the contaminant load to be processed by the charcoal bed filter 26 . Such action may allow for a relatively small charcoal bed filter 26 .
- the acid water wash sprayed into the acid water scrubber 60 may act to control temperature and humidity by the use of a cold acid water wash in the temperature range of about 40 to 60° F.
- the cooling occurs due to direct thermal contact when cool acid water is sprayed into the air flow.
- the large surface area of the spray that may be effective for mass transfer may also be effective for heat transfer. Water vapor in the air may condense in the cold acid water spray and then be separated by the centrifugal action of the acid water scrubber 60 to adjust the humidity.
- the resultant dilute acid water may then be accumulated in acid water tank 62 .
- As part of the process water may be removed from the acid water tank and acid may be added to maintain proper pH for reuse in the acid water scrubber 60 .
- the removed dilute acid water may have salts and dissolved trace gasses. It may be processed in a water recovery system in the host vehicle for reuse in the water cycle. Processed acid water may be cooled at acid water cooler 64 and introduced to the acid water scrubber 60 .
- the carbon dioxide rich liquid absorbent solution may also be processed for reuse in the carbon dioxide scrubber 40 .
- the liquid absorbent solution may be heated and processed through the stripper element 80 to separate carbon dioxide from the liquid absorbent solution.
- the carbonate complexes formed in the scrubber during the absorption of carbon dioxide are thermally unstable, for example, methanol amine carbonate decomposes at 270° F.
- Approximately five percent of the flow of liquid absorbent used to treat the air in the scrubber 30 may be heated in liquid absorbent heater 44 and introduced into the stripper 80 .
- the stripper 80 may be a rotary contact processor similar to the rotary contact processor 32 .
- the stripper 80 permits evolution of the carbon dioxide and the separation of the liquid phase.
- the method for the process using a rotary contact processor comprises the steps of heating the carbonate rich liquid absorbent to its decomposition temperature in a flow through liquid absorbent heater, communicating the heated liquid absorbent into a first stage scrubber and spraying the heated liquid absorbent onto a rotating heat and mass transfer surface thereby separating the liquid absorbent from the evolved carbon dioxide gas through centrifugal action, accumulating the carbonate lean liquid absorbent and removing it from the transfer surface using pitot pumps, and passing the carbon dioxide gas through a plurality of mist separators for removal of droplets prior to being output.
- the carbon dioxide gas may be further processed by introduction into a second stage scrubber to remove water and absorbent vapors.
- the carbon dioxide gas may be washed by a spray of a cold liquid absorbent that may then be sprayed onto a rotating mass and heat transfer surface, the liquid absorbent separation from the carbon dioxide may be caused by centrifugal action, the liquid absorbent may then be accumulated and then removed by pitot pumps, and the carbon dioxide may be passed through a plurality of mist separators for removal of droplets prior to being output.
- the liquid absorbent may be first processed by a stripper element 80 to remove carbonate complexes present in the solution.
- the heated liquid absorbent may be sprayed into the stripper element 80 , which may be a rotary contact processor wherein the small droplets formed provide a large surface area permitting efficient carbon dioxide transfer.
- the pressure of the carbon dioxide may be controlled as for example by using a back-pressure regulating valve. Depending on the liquid absorbent used, the pressure can be set in the range of 40 to 70 psi.
- the rotary stripper element 80 centrifugal action functions to separate the liquid and gas phases similar to the scrubber 30 .
- the resultant carbon dioxide vapor may be hot and contain water vapor and absorbent vapor.
- the vapors are removed in a stripper element 80 by cooling the carbon dioxide and condensing the liquid.
- the cool liquid absorbent solution may be returned to the liquid absorbent tank 42 and the carbon dioxide may be compressed, dried and stored for further use or disposal.
- the scrubber 30 rotary contact processor 32 functions to provide direct liquid contact between air and two separate liquids, to separate the liquids and air, and to pump the liquids.
- the rotary contact processor 32 may be a dual rotor ambient pressure air scrubber that washes the air in the carbon dioxide scrubber rotor 104 with a carbon dioxide absorbent and washes the air with mild acid in the liquid absorbent scrubber rotor 107 as air flows through the device. It is supplied with a liquid absorbent solution, cooled acid wash water, atmospheric air, and electrical power. Electrical power is used for a drive motor, not shown.
- the advantage of this device is that it operates at atmospheric pressure, it is gravity independent and it provides a simple, rugged device.
- the contact processor 32 consists of a rotor assembly comprised of carbon dioxide scrubber rotor 104 and liquid absorbent scrubber rotor 107 mounted in a housing 116 on bearings 120 . Scrubbing and separation occur within the rotor. Liquid absorbent solution may be circulated through connections 102 , 118 in the stationary hub 122 at one end and cooled acid wash water may be circulated through connections 105 , 114 in a stationary baffle 115 located in the middle of the housing.
- the two rotors 104 , 107 are mounted on shaft 110 and are separated by stationary baffle 115 .
- the first rotor 104 is in the carbon dioxide scrubber chamber 124 and may be used to remove carbon dioxide from the air stream.
- the second rotor 107 is in the acid wash scrubber chamber 126 and may be used to wash the air and to condense water from the air stream. Mist separators 111 and baffles 115 are used to isolate the two fluids.
- the air may be moved through the rotary contact processor 32 by a built-in fan 112 . An external blower, not shown, may also be used.
- the rotary contact processor 32 operates in the following manner: atmospheric air flows in the inlet 101 past the carbon dioxide scrubber rotor 104 , through air passage tubes 109 and mist separators 111 , past the liquid absorbent scrubber rotor 107 , through second air passage tubes 109 and second mist separators 111 , and through the fan 112 , to the air exhaust 108 .
- the fan 112 moves the air through the rotary contact processor 32 and the drive motor, not shown, keeps the rotors and fan moving at constant speed.
- Carbon dioxide is removed from the air stream in the carbon dioxide scrubber chamber 124 .
- Liquid absorbent enters at connection 118 and is sprayed into the air stream near the axis of rotation 128 . It forms droplets and a thin layer on the carbon dioxide scrubber rotor 104 heat and mass transfer surface 117 .
- the liquid flows by centrifugal action to the outside of the carbon dioxide scrubber chamber 124 . This direct contact promotes the rapid absorption of carbon dioxide by the liquid absorbent.
- a mist separator 111 keeps liquid absorbent from entering the next chamber.
- the liquid absorbent forms a layer on the periphery of the chamber 124 and is pumped by the liquid absorbent pitot pump 103 through the liquid absorbent outlet 102 to an external liquid absorbent tank 42 .
- the return liquid absorbent enters through liquid absorbent inlet 118 .
- the air is washed, cooled and humidity condensed in the acid wash scrubber chamber 126 .
- Cold acid wash enters through the acid water wash inlet 114 and is sprayed into the air stream near the axis of rotation 128 . It forms droplets and a thin layer on the liquid absorbent scrubber rotor 107 transfer surface 117 .
- the liquid flows by centrifugal action to the outside of the acid wash scrubber chamber 126 and a portion of the humidity in the air stream condenses.
- the air stream is cooled below the dew point by the cold acid water wash.
- a mist separator 111 keeps water droplets from entering the exhaust stream at air exhaust 108 .
- the condensate liquid forms a layer on the periphery of the chamber 126 and is pumped by the acid water pitot pump 106 through the acid water wash outlet 105 to the external circuit.
- the return cold acid water wash enters through the acid water wash inlet 114 .
- An inventive method 200 is illustrated in a flow chart of FIG. 4 .
- a flow of cabin air is introduced into a carbon dioxide scrubber.
- a liquid mist is sprayed into the introduced air in order to modify its temperature, humidity and carbon dioxide concentration.
Abstract
An integrated environmental control system for cabin air of an aircraft or spacecraft. Humidity and temperature of cabin air are controlled with a direct contact liquid air contaminant control system that revitalizes cabin air by removal of carbon dioxide and other trace gas contaminants through use of a direct contact air, liquid scrubber element and stripper element. The scrubber element has two rotor elements rotatably mounted in a housing first for centrifugal separation of an air flow and liquid absorbent mixture which liquid absorbent has absorbed carbon dioxide and trace gas contaminants. Then second for centrifugal separation of an air flow and acid water wash mixture which acid water wash has liquid absorbent and other contaminants. The processed air is then passed through a charcoal bed filter for further removal of contaminants. A rotary contact processor may also be used to reprocess contaminated liquid absorbent for reuse.
Description
- This application is a continuation-in-part of Ser. No. 10/611,490 filed Jun. 30, 2003.
- The present invention generally relates to an air environment control system (ECS) that revitalizes air and more specifically to the apparatus and methods that control humidity and temperature of cabin air of aircraft and spacecraft while removing carbon dioxide and other trace gas contaminates.
- Liquid amine (methanol amine water solutions) based carbon dioxide and trace gas contaminant removal apparatus and processes for regeneration of air have been used in nuclear submarines for over forty years. Such systems are used to remove carbon dioxide for the breathing air and depend on gravity to process the liquid carbon amine or other liquids and air mixture.
- An example of a combustion gas carbon dioxide process and apparatus is disclosed in U.S. Pat. No. 5,318,758. This type of gas process involves towers and other structures that depend on gravity, blowers and pumps to process the gas. Such systems are not simple or compact and do not work in reduced gravity environments such as on aircraft and spacecraft.
- The use of alternative absorbent solutions has been disclosed in U.S. Pat. Nos. 4,285,918 and 3,632,519. These patents teach that water solutions of 3-amino-1,2-propanediol and ω-aminomethyl alkyl sulfone have improved performance for carbon dioxide removal in closed environments such as submarines. They address only the removal of carbon dioxide whereas there are a number of other contaminants that must be removed in these closed environments.
- Centrifugal liquid and gas processors have been explored as described in the article “The Centrifugal Mass Exchange Apparatus in Air-Conditioning System of Isolated, Inhabited Object and Its Work Control”, by P. A. Barabash, et al, in Proceedings of the 4th European Symposium on Space Environmental and Control Systems, Oct. 21-24, 1991. The article postulates use of a centrifugal apparatus to work with an air-conditioning system in a closed habitat system such as an orbital space station. A single stage system is proposed that keeps air temperature and humidity parameters within limits. The single stage rotor does not anticipate a more staged air process system using contaminant absorbent fluids and acid wash to provide carbon dioxide and other contaminant removal from a cabin air environment. Indeed, present spacecraft and space stations typically employ apparatus dedicated exclusively to contaminant extraction from cabin air. Another apparatus is used for maintaining humidity and temperature of the cabin air. Each of these independent systems adds undesirable weight and consumes valuable space and power in a spacecraft.
- As can be seen, there is a need for a simple, compact ECS in which humidity and temperature control are integrated with air regeneration functions for use in aircraft and spacecraft.
- An improved environmental control system and method according to the present invention may comprise a carbon dioxide scrubber, a liquid absorbent stripper, a charcoal filter, and supporting containers, pumps and other elements.
- In one aspect of the present invention, method for providing environmental control for cabin air of a vehicle comprises the steps of introducing a portion of the cabin air as air flow into a carbon dioxide scrubber and spraying a liquid mist into the air flow thereby modifying humidity, temperature and carbon dioxide concentration of the cabin air.
- In another aspect of the present invention, an environmental control apparatus for cabin air of a vehicle comprises a contaminant scrubber wherein a contamination-control liquid is introduced as a mist into an air flow of a portion of the cabin air through the contaminant scrubber. The contamination-control liquid has a temperature lower than a temperature of the cabin air. Temperature of the cabin air is reduced and humidity of the cabin air is modified.
- In another aspect of the present invention, an apparatus for controlling humidity and temperature of cabin air in a vehicle comprises a rotary contact processor for direct contact liquid absorbent and gas contaminant processing.
- These and other features, aspects and advantages of the present invention will become better understood with reference to the following drawings, description and claims.
-
FIG. 1 illustrates a functional block diagram of the invention; -
FIG. 2 illustrates a functional block diagram of the major elements according to an embodiment of the invention; -
FIG. 3 illustrates a functional cross-sectional view of a rotary liquid contact processor apparatus according to an embodiment of the invention; and -
FIG. 4 is a flow chart of a method for providing environmental control for cabin air of a vehicle according to an embodiment of the invention. - The following detailed description is of the best currently contemplated modes of carrying out the invention. The description is not to be taken in a limiting sense, but is made merely for the purpose of illustrating the general principles of the invention, since the scope of the invention is best defined by the appended claims.
- Referring to
FIGS. 1 and 2 , an environmental control system (ECS) 10 has anabsorber element 20 and astripper element 80 in fluid communication and in control/data communication. Support elements such as a control and data processor and an electric power source, not shown, are provided by existing platform equipment as is found on spacecraft and aircraft. The ECS 10 may be connected to the cabin air system of a vehicle to process the return air from use in a vehicle human environment, to decontaminate, cool and dehumidify the air, and to return cold clean air for use in a continuing cycle. - The current
system absorber element 20 uses arotary process scrubber 30 andcharcoal bed filter 26 to remove contaminants. Both liquid absorbent (such as an amine) and acid water are used in thescrubber 30 for direct contact liquid/vapor phase separation of contaminants. Thestripper 80 may also use a rotary processor for liquid/vapor phase separation of liquid absorbent and carbon dioxide. The use of rotary processors allows operation in variable gravity environments such as experienced in aircraft and spacecraft and provides compact, light weight and reliable apparatus as compared to current art bulky, inefficient apparatus. In addition, the use of direct contact liquid/vapor processing allows more efficient heat transfer as compared to current technology, which relies on use of condensing heat exchangers, slurpers, and rotating centrifugal phase separators. A cold contamination-control liquid such as an acid water spray may be used in the air contaminant control system to remove absorbent vapor from the air and for temperature and humidity control. As cabin air is introduced into theECS 10, and passes through the cold spray the air temperature may be reduced. The air may become saturated as it is cooled toward the temperature of the acid water and some of the moisture conveyed in the air may condense and mix with the acid water. Thus moisture content of the air may diminish. If the air does not become saturated with water as it is cooled to the temperature of the acid water spray, water may evaporate from the cold acid water spray and add the water content of the air. Additionally, cabin air may be cooled as it passes through the cold water spray. These humidity adjustment and cooling functions may be an integral part of the direct liquid contact system and not a separate system. For the presentinventive ECS 10 control of humidity may be the design limiting function of the system. The ECS 10 may be sized to process enough air to control the humidity. By doing so, the other functions, such as temperature control and contamination control, may be easily satisfied. - Cabin air may be drawn through the
scrubber 30 by a fan that may be used to aid vehicle cabin ventilation air flow. In thescrubber 30 carbon dioxide and other contaminates may be removed from the air through direct contact with a cool liquid absorbent. The liquid absorbent removes carbon dioxide to form a carbonate complex. The term liquid absorbent as commonly understood in the art relates to carbon dioxide liquid absorbents, as for example, water solutions of methanol amine, ethanol amine, isopropyl amine, cesium carbonate, magnesium carbonate and similar solutions. The choice of liquid absorbent may be based on system operational factors such as carbon dioxide pressure, temperature, humidity, regeneration temperature and energy sources. - The amines have a low vapor pressure at absorption conditions; however, without treatment some amine vapor may remain in the processed air to be introduced into the vehicle cabin as a contaminant. To inhibit this event an
acid water scrubber 60 may be included in thescrubber 30 to maintain amine pressure at acceptable levels, for example, about 1 ppm. The same process may absorb other basic trace gases such as ammonia. A mild acid, such as, citric, acetic, or hypo-phosphoric acid, may reduce the amine vapor pressure to the desired levels. Additionally, the acid water may serve as an anti-microbial with the potential for reducing bacterial contamination or spread of pathogens. The acid water solution may become very diluted, but the pH should be maintained relatively low, i.e., less than about 2 value. Additional acid may be added to theacid water scrubber 60 to maintain a low pH. For a fully closed system acetic acid, vinegar, may be produced onboard a vehicle using well known biological processes. - The
carbon dioxide scrubber 40 may act to absorb acidic trace gases. The combination of thecarbon dioxide scrubber 40 andacid water scrubber 60 results in substantial removal of water soluble trace gases. There may also be hydrocarbon trace gasses in the air that may not be absorbed in thescrubber 30. These gases may be removed by acharcoal bed filter 26 downstream of thescrubber 30. Thecharcoal bed filter 26 may be a single use or regenerable device depending on the mission requirements. Generally large portions of the trace contaminants are removed in thescrubber 30 thereby reducing the contaminant load to be processed by thecharcoal bed filter 26. Such action may allow for a relatively smallcharcoal bed filter 26. - The acid water wash sprayed into the
acid water scrubber 60 may act to control temperature and humidity by the use of a cold acid water wash in the temperature range of about 40 to 60° F. The cooling occurs due to direct thermal contact when cool acid water is sprayed into the air flow. The large surface area of the spray that may be effective for mass transfer may also be effective for heat transfer. Water vapor in the air may condense in the cold acid water spray and then be separated by the centrifugal action of theacid water scrubber 60 to adjust the humidity. - The resultant dilute acid water may then be accumulated in
acid water tank 62. As part of the process water may be removed from the acid water tank and acid may be added to maintain proper pH for reuse in theacid water scrubber 60. The removed dilute acid water may have salts and dissolved trace gasses. It may be processed in a water recovery system in the host vehicle for reuse in the water cycle. Processed acid water may be cooled atacid water cooler 64 and introduced to theacid water scrubber 60. - The carbon dioxide rich liquid absorbent solution may also be processed for reuse in the
carbon dioxide scrubber 40. The liquid absorbent solution may be heated and processed through thestripper element 80 to separate carbon dioxide from the liquid absorbent solution. The carbonate complexes formed in the scrubber during the absorption of carbon dioxide are thermally unstable, for example, methanol amine carbonate decomposes at 270° F. Approximately five percent of the flow of liquid absorbent used to treat the air in thescrubber 30 may be heated in liquidabsorbent heater 44 and introduced into thestripper 80. Thestripper 80 may be a rotary contact processor similar to therotary contact processor 32. - The
stripper 80 permits evolution of the carbon dioxide and the separation of the liquid phase. The method for the process using a rotary contact processor comprises the steps of heating the carbonate rich liquid absorbent to its decomposition temperature in a flow through liquid absorbent heater, communicating the heated liquid absorbent into a first stage scrubber and spraying the heated liquid absorbent onto a rotating heat and mass transfer surface thereby separating the liquid absorbent from the evolved carbon dioxide gas through centrifugal action, accumulating the carbonate lean liquid absorbent and removing it from the transfer surface using pitot pumps, and passing the carbon dioxide gas through a plurality of mist separators for removal of droplets prior to being output. - The carbon dioxide gas may be further processed by introduction into a second stage scrubber to remove water and absorbent vapors. The carbon dioxide gas may be washed by a spray of a cold liquid absorbent that may then be sprayed onto a rotating mass and heat transfer surface, the liquid absorbent separation from the carbon dioxide may be caused by centrifugal action, the liquid absorbent may then be accumulated and then removed by pitot pumps, and the carbon dioxide may be passed through a plurality of mist separators for removal of droplets prior to being output.
- In each case of the liquid absorbent and the carbon dioxide processing, more process stages may be used to obtain desired absorbent regeneration and product carbon dioxide purity.
- The liquid absorbent may be first processed by a
stripper element 80 to remove carbonate complexes present in the solution. The heated liquid absorbent may be sprayed into thestripper element 80, which may be a rotary contact processor wherein the small droplets formed provide a large surface area permitting efficient carbon dioxide transfer. The pressure of the carbon dioxide may be controlled as for example by using a back-pressure regulating valve. Depending on the liquid absorbent used, the pressure can be set in the range of 40 to 70 psi. Therotary stripper element 80 centrifugal action functions to separate the liquid and gas phases similar to thescrubber 30. - The resultant carbon dioxide vapor may be hot and contain water vapor and absorbent vapor. The vapors are removed in a
stripper element 80 by cooling the carbon dioxide and condensing the liquid. The cool liquid absorbent solution may be returned to the liquidabsorbent tank 42 and the carbon dioxide may be compressed, dried and stored for further use or disposal. - Referring to
FIGS. 2 and 3 , thescrubber 30rotary contact processor 32 functions to provide direct liquid contact between air and two separate liquids, to separate the liquids and air, and to pump the liquids. Therotary contact processor 32 may be a dual rotor ambient pressure air scrubber that washes the air in the carbondioxide scrubber rotor 104 with a carbon dioxide absorbent and washes the air with mild acid in the liquidabsorbent scrubber rotor 107 as air flows through the device. It is supplied with a liquid absorbent solution, cooled acid wash water, atmospheric air, and electrical power. Electrical power is used for a drive motor, not shown. The advantage of this device is that it operates at atmospheric pressure, it is gravity independent and it provides a simple, rugged device. - The
contact processor 32 consists of a rotor assembly comprised of carbondioxide scrubber rotor 104 and liquidabsorbent scrubber rotor 107 mounted in ahousing 116 onbearings 120. Scrubbing and separation occur within the rotor. Liquid absorbent solution may be circulated throughconnections stationary hub 122 at one end and cooled acid wash water may be circulated throughconnections stationary baffle 115 located in the middle of the housing. - The two
rotors shaft 110 and are separated bystationary baffle 115. Thefirst rotor 104 is in the carbondioxide scrubber chamber 124 and may be used to remove carbon dioxide from the air stream. Thesecond rotor 107 is in the acid washscrubber chamber 126 and may be used to wash the air and to condense water from the air stream.Mist separators 111 and baffles 115 are used to isolate the two fluids. The air may be moved through therotary contact processor 32 by a built-infan 112. An external blower, not shown, may also be used. - The
rotary contact processor 32 operates in the following manner: atmospheric air flows in theinlet 101 past the carbondioxide scrubber rotor 104, throughair passage tubes 109 andmist separators 111, past the liquidabsorbent scrubber rotor 107, through secondair passage tubes 109 andsecond mist separators 111, and through thefan 112, to theair exhaust 108. Thefan 112 moves the air through therotary contact processor 32 and the drive motor, not shown, keeps the rotors and fan moving at constant speed. - Carbon dioxide is removed from the air stream in the carbon
dioxide scrubber chamber 124. Liquid absorbent enters atconnection 118 and is sprayed into the air stream near the axis of rotation 128. It forms droplets and a thin layer on the carbondioxide scrubber rotor 104 heat andmass transfer surface 117. The liquid flows by centrifugal action to the outside of the carbondioxide scrubber chamber 124. This direct contact promotes the rapid absorption of carbon dioxide by the liquid absorbent. Amist separator 111 keeps liquid absorbent from entering the next chamber. The liquid absorbent forms a layer on the periphery of thechamber 124 and is pumped by the liquidabsorbent pitot pump 103 through the liquidabsorbent outlet 102 to an external liquidabsorbent tank 42. The return liquid absorbent enters through liquidabsorbent inlet 118. - The air is washed, cooled and humidity condensed in the acid wash
scrubber chamber 126. Cold acid wash enters through the acidwater wash inlet 114 and is sprayed into the air stream near the axis of rotation 128. It forms droplets and a thin layer on the liquidabsorbent scrubber rotor 107transfer surface 117. The liquid flows by centrifugal action to the outside of the acid washscrubber chamber 126 and a portion of the humidity in the air stream condenses. The air stream is cooled below the dew point by the cold acid water wash. Amist separator 111 keeps water droplets from entering the exhaust stream atair exhaust 108. The condensate liquid forms a layer on the periphery of thechamber 126 and is pumped by the acidwater pitot pump 106 through the acidwater wash outlet 105 to the external circuit. The return cold acid water wash enters through the acidwater wash inlet 114. - While one embodiment is described in terms of a two
stage scrubber 30 having acarbon dioxide scrubber 40 and a liquidabsorbent scrubber 60 having a common rotor shaft and housing, these two elements may also be contained in separate housings with fluid communication therebetween. In such an instance, thebaffle 115 would be separated in structure such that thecarbon dioxide scrubber 40 would have an outlet enclosed side and the liquidabsorbent scrubber 60 would have an inlet enclosed side. Also, more than two stages may be used depending on the purity of the output desired by the user. - An
inventive method 200 is illustrated in a flow chart ofFIG. 4 . In astep 202, a flow of cabin air is introduced into a carbon dioxide scrubber. In astep 204, a liquid mist is sprayed into the introduced air in order to modify its temperature, humidity and carbon dioxide concentration. - It should be understood, of course, that the foregoing relates to preferred embodiments of the invention and that modifications may be made without departing from the spirit and scope of the invention as set forth in the following claims.
Claims (20)
1. A method for providing environmental control for cabin air of a vehicle comprising the steps of:
introducing a portion of the cabin air as air flow into a carbon dioxide scrubber; and
spraying a liquid mist into the air flow thereby modifying humidity, temperature and carbon dioxide concentration of the cabin air.
2. The method of claim 1 wherein the liquid mist is an acid wash.
3. The method of claim 1 comprising the further steps of:
rotating a carbon dioxide scrubber rotor to separate liquid absorbent containing absorbed carbon dioxide and trace contaminants from the air flow;
accumulating the liquid absorbent on a first heat and mass transfer surface for extraction from the carbon dioxide scrubber rotor;
passing the air flow downstream of the carbon dioxide scrubber rotor through a plurality of first air passages and a plurality of first mist separators to a liquid absorbent scrubber rotor.
4. The method of claim 3 comprising the further steps of;
rotating the liquid absorbent scrubber rotor to separate the liquid absorbent containing carbon dioxide and trace contaminants from the air flow;
accumulating the acid wash on a second heat and mass transfer surface for extraction from the liquid absorbent scrubber rotor; and
passing air flow downstream of the liquid absorbent scrubber rotor through a fan to an air exhaust.
5. The method of claim 3 wherein extracted liquid absorbent is processed in a stripper element for reuse.
6. The method of claim 3 wherein contaminated liquid absorbents are reconditioned by performing the steps of:
heating a liquid absorbent containing a carbonate to a decomposition temperature in a liquid absorbent heater whereby carbon dioxide is separated from the liquid absorbent.
7. The method of claim 6 wherein the liquid absorbent is processed through a subsequent scrubber.
8. The method of claim 6 further comprising the steps of:
communicating the carbon dioxide which is separated from the liquid absorbent into a second scrubber;
washing the carbon dioxide using a spray of cold liquid absorbent;
accumulating the cold liquid absorbent for extraction from the second scrubber; and
passing the carbon dioxide through a plurality of mist separators for output from the second scrubber.
9. An environmental control apparatus for cabin air of a vehicle comprising:
a contaminant scrubber wherein a contamination-control liquid is introduced as a mist into an air flow of a portion of the cabin air through the contaminant scrubber;
the contamination-control liquid having a temperature lower than a temperature of the cabin air; and
wherein temperature of the cabin air is reduced and humidity of the cabin air is modified.
10. The environmental control apparatus as in claim 9 wherein the contaminant scrubber is comprised of at least one carbon dioxide scrubber in fluid communication with a liquid absorbent scrubber.
11. The environmental control apparatus as in claim 10 wherein the at least one carbon dioxide scrubber comprises a rotary contact processor.
12. The environmental control apparatus as in claim 11 further comprising a stripper element which comprises a rotary contact processor.
13. The environmental control apparatus as in claim 9 wherein:
a carbon dioxide scrubber rotor is connected to a liquid absorbent scrubber rotor by a rotor shaft;
the carbon dioxide scrubber rotor is in communication with an air inlet and a liquid absorbent inlet wherein a liquid absorbent is introduced as a mist into an air flow through the air inlet, the air flow introduced into a carbon dioxide scrubber chamber having a first heat and mass transfer surface therein of the carbon dioxide scrubber rotor;
the air flow passes through the carbon dioxide scrubber rotor through a plurality of first air passage tubes and a plurality of first mist separators to be introduced downstream into an acid wash scrubber chamber having a second heat and mass transfer surface therein;
the acid wash scrubber is separated from the carbon dioxide scrubber rotor with a baffle;
the baffle has an acid water wash inlet for introduction of a liquid acid water wash as a mist in the air flow; and
the air flow passes through the liquid absorbent scrubber rotor through a plurality of second air passage tubes and a plurality of second mist separators to a fan causing the air flow to exit through an air exhaust.
14. Apparatus for controlling humidity and temperature of cabin air in a vehicle comprising:
a rotary contact processor for direct contact liquid absorbent and gas contaminant processing.
15. The apparatus of claim 14 wherein the rotary contact processor comprises:
a first scrubber rotor in communication with a gas inlet and a liquid absorbent inlet, wherein a liquid absorbent is introduced as a mist into a gas flow through the gas inlet.
16. The apparatus of claim 15 wherein the liquid absorbent inlet and a liquid absorbent outlet are in communication with a liquid absorbent tank, a liquid absorbent heater and a stripper element.
17. The apparatus of claim 16 wherein an acid water wash inlet and an acid water wash outlet are in communication with an acid water tank and an acid water cooler.
18. The apparatus of claim 14 wherein:
a first scrubber rotor is in serial communication with a second scrubber rotor each assembled on a rotor shaft rotatably mounted on a plurality of bearings in a housing; and
gas flow passes through the first scrubber rotor through a plurality of first gas passage tubes and a plurality of first mist separators to be introduced downstream into a second scrubber chamber in fluid communication therewith and having a second heat and mass transfer surface therein.
19. The apparatus of claim 18 wherein:
the second scrubber chamber has a liquid absorbent wash inlet for introduction of a liquid absorbent wash as a mist in the gas flow; and
the gas flow passes through the liquid absorbent scrubber rotor through a plurality of second gas passage tubes and a plurality of second mist
separators to a fan causing the gas flow to exit the rotary contact processor through a gas exhaust.
20. The apparatus of claim 19 further comprising a first pitot pump in a first scrubber chamber for liquid absorbent wash circulation and exit through a liquid absorbent outlet.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/741,686 US20080112869A1 (en) | 2003-06-30 | 2007-04-27 | Direct contact liquid air contaminant control system |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/611,490 US7252703B2 (en) | 2003-06-30 | 2003-06-30 | Direct contact liquid air contaminant control system |
US11/741,686 US20080112869A1 (en) | 2003-06-30 | 2007-04-27 | Direct contact liquid air contaminant control system |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/611,490 Continuation-In-Part US7252703B2 (en) | 2003-06-30 | 2003-06-30 | Direct contact liquid air contaminant control system |
Publications (1)
Publication Number | Publication Date |
---|---|
US20080112869A1 true US20080112869A1 (en) | 2008-05-15 |
Family
ID=33541328
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/611,490 Expired - Fee Related US7252703B2 (en) | 2003-06-30 | 2003-06-30 | Direct contact liquid air contaminant control system |
US11/741,686 Abandoned US20080112869A1 (en) | 2003-06-30 | 2007-04-27 | Direct contact liquid air contaminant control system |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/611,490 Expired - Fee Related US7252703B2 (en) | 2003-06-30 | 2003-06-30 | Direct contact liquid air contaminant control system |
Country Status (2)
Country | Link |
---|---|
US (2) | US7252703B2 (en) |
WO (1) | WO2005005026A1 (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20070243119A1 (en) * | 2006-04-13 | 2007-10-18 | William Downs | Process for controlling the moisture concentration of a combustion flue gas |
US20110135550A1 (en) * | 2009-12-03 | 2011-06-09 | Mitsubishi Heavy Industries, Ltd. | Co2 recovery system and co2 recovery method |
US20110158891A1 (en) * | 2009-12-25 | 2011-06-30 | Mitsubishi Heavy Industries, Ltd. | Co2 recovery system and co2 recovery method |
RU2505341C1 (en) * | 2012-06-15 | 2014-01-27 | Общество с ограниченной ответственностью "НПО Пылеочистка" | Method of gas cleaning |
CN103920396A (en) * | 2014-03-31 | 2014-07-16 | 煤科集团杭州环保研究院有限公司 | Automatic open-type double-alkali-method desulphurized gypsum oxidation system and control method thereof |
CN109420407A (en) * | 2017-08-31 | 2019-03-05 | 双叶产业株式会社 | The method of carbon dioxide contained in carbon dioxide application equipment and recycling burning waste gas |
US11852062B2 (en) * | 2020-10-13 | 2023-12-26 | Daewoo Shipbuilding & Marine Engineering Co., Ltd. | Apparatus for reducing greenhouse gas emission in vessel and vessel including the same |
Families Citing this family (35)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7976803B2 (en) * | 2005-08-16 | 2011-07-12 | Co2Crc Technologies Pty Ltd. | Plant and process for removing carbon dioxide from gas streams |
ES2440804T3 (en) * | 2006-03-10 | 2014-01-30 | C-Quest Technologies International Llc | Carbon dioxide sequestration procedure |
US7628845B2 (en) * | 2006-03-10 | 2009-12-08 | Macronix International Co., Ltd. | Filtering device and filtering method thereof and semiconductor fabricating method |
CN101553430A (en) * | 2006-08-29 | 2009-10-07 | 耶德研究和发展有限公司 | Methods and apparatuses for decreasing the CO2 concentration of a fluid |
US7993616B2 (en) * | 2007-09-19 | 2011-08-09 | C-Quest Technologies LLC | Methods and devices for reducing hazardous air pollutants |
NO332812B1 (en) * | 2009-03-13 | 2013-01-21 | Aker Clean Carbon As | Amine emission control |
NO332547B1 (en) * | 2009-07-10 | 2012-10-22 | Statoil Asa | Compact absorption-desorption process using concentrated solution |
US9038409B2 (en) * | 2009-09-21 | 2015-05-26 | Korea Research Institute Of Chemical Technology | Apparatus for treating air by using porous organic-inorganic hybrid materials as an absorbent |
FR2958180A1 (en) * | 2010-04-06 | 2011-10-07 | Inst Francais Du Petrole | Capturing acid compounds comprising carbon dioxide and hydrogen sulfide contained in e.g. natural gas, comprises contacting gas with absorbent solution, and regenerating fraction of absorbent solution enriched in acid compounds |
US7988909B1 (en) * | 2010-05-20 | 2011-08-02 | Ying Gang Ruan | Method and apparatus for conditioning room air |
US20110296985A1 (en) * | 2010-06-01 | 2011-12-08 | Shell Oil Company | Centrifugal force gas separation with an incompressible fluid |
US8858680B2 (en) | 2010-06-01 | 2014-10-14 | Shell Oil Company | Separation of oxygen containing gases |
US8858679B2 (en) | 2010-06-01 | 2014-10-14 | Shell Oil Company | Separation of industrial gases |
US8663369B2 (en) | 2010-06-01 | 2014-03-04 | Shell Oil Company | Separation of gases produced by combustion |
EP2576018A1 (en) | 2010-06-01 | 2013-04-10 | Shell Oil Company | Low emission power plant |
JP5585873B2 (en) * | 2010-09-03 | 2014-09-10 | 独立行政法人産業技術総合研究所 | Environmental purification method and apparatus using ionic liquid |
NO333941B1 (en) | 2010-12-09 | 2013-10-28 | Statoil Petroleum As | PROCEDURE AND ABSORBES FOR REMOVAL OF ACID GAS FROM NATURAL GAS |
WO2012092981A1 (en) * | 2011-01-07 | 2012-07-12 | Statoil Petroleum As | Method and absorber for removal of a contaminant from natural gas |
ES2616028T3 (en) * | 2011-01-20 | 2017-06-09 | Saudi Arabian Oil Company | Reversible adsorption method on solid and system that uses residual heat for recovery and storage on board CO2 |
US8728210B2 (en) * | 2011-07-07 | 2014-05-20 | Hsueh Yuan Lee | Exhaust gas treatment apparatus and method |
EP3068510B1 (en) * | 2013-10-22 | 2019-09-11 | Compact Carbon Capture AS | System and process for absorption and desorption of co2 |
WO2015060724A1 (en) * | 2013-10-22 | 2015-04-30 | Statoil Petroleum As | Apparatus and method for absorbing co2 from flue gas |
KR101534710B1 (en) * | 2013-11-12 | 2015-07-07 | 현대자동차 주식회사 | Device for absorbing and separating acid gases |
US9108146B1 (en) * | 2014-06-02 | 2015-08-18 | Stephen Waco Jackson | System for removing particulate matter from dirty air |
CN106310902A (en) * | 2015-06-29 | 2017-01-11 | 颜声林 | Waste gas treatment device |
US10507425B2 (en) | 2016-08-24 | 2019-12-17 | Honeywell International Inc. | Ionic liquid CO2 scrubber for spacecraft |
US11123685B2 (en) | 2017-02-27 | 2021-09-21 | Honeywell International Inc. | Hollow fiber membrane contactor scrubber/stripper for cabin carbon dioxide and humidity control |
US10941497B2 (en) * | 2017-02-27 | 2021-03-09 | Honeywell International Inc. | Electrochemical carbon dioxide converter and liquid regenerator |
US10688435B2 (en) * | 2017-02-27 | 2020-06-23 | Honeywell International Inc. | Dual stripper with water sweep gas |
CN107126796B (en) * | 2017-06-28 | 2019-09-03 | 太原理工大学 | A kind of air water washing cleaning unit |
CN109364696B (en) * | 2018-11-21 | 2021-06-04 | 周国梁 | High-efficient gas purification equipment |
CN110124494A (en) * | 2019-05-16 | 2019-08-16 | 扬州绿泉环保工程技术有限公司 | A kind of high-temperature waste gas treating apparatus |
US11612855B2 (en) * | 2021-03-24 | 2023-03-28 | Next Carbon Solutions, Llc | Processes, apparatuses, and systems for direct air carbon capture utilizing waste heat and exhaust air |
CN113446245B (en) * | 2021-07-21 | 2022-03-11 | 徐瑶 | Centrifugal ventilator for acid mist waste gas purification tower |
CN115608128A (en) * | 2022-08-27 | 2023-01-17 | 领航国创等离子研究院(阜阳)有限公司 | Industrial flue gas carbon dioxide capturing and converting method and application |
Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3632519A (en) * | 1969-11-10 | 1972-01-04 | Us Navy | Aqueous solutions of omega-aminoalkyl alkylsulfones as regenerative co2 absorbents |
US3727375A (en) * | 1971-08-12 | 1973-04-17 | R Wallace | Continuous electromigration process for removal of gaseous contaminants from the atmosphere and apparatus |
US3969094A (en) * | 1973-12-11 | 1976-07-13 | E. I. Du Pont De Nemours And Company | Flue gas scrubber |
US4285918A (en) * | 1980-02-25 | 1981-08-25 | The United States Of America As Represented By The Secretary Of The Navy | Regenerative CO2 absorbent |
US4375975A (en) * | 1980-06-04 | 1983-03-08 | Mgi International Inc. | Centrifugal separator |
US4810266A (en) * | 1988-02-25 | 1989-03-07 | Allied-Signal Inc. | Carbon dioxide removal using aminated carbon molecular sieves |
US5318758A (en) * | 1991-03-07 | 1994-06-07 | Mitsubishi Jukogyo Kabushiki Kaisha | Apparatus and process for removing carbon dioxide from combustion exhaust gas |
US5876486A (en) * | 1995-09-09 | 1999-03-02 | Dornier Gmbh | Method and apparatus for removing carbon dioxide |
US6132493A (en) * | 1998-08-05 | 2000-10-17 | Church; C. Daniel | Apparatus and method for washing air with a liquid without an eliminator |
US6190629B1 (en) * | 1999-04-16 | 2001-02-20 | Cbl Technologies, Inc. | Organic acid scrubber and methods |
US6258215B1 (en) * | 1998-07-21 | 2001-07-10 | Otkrytoe aktsionernoe obschestvo “Nauchno-Issledovatelsky I Konstruktosky Institut Kkhimicheskogo Mashinostroenia (A. O. Neikhimmash”) | System and a rotary vacuum distiller for water recovery from aqueous solutions, preferably from urine aboard spacecraft |
US6364940B1 (en) * | 1994-11-10 | 2002-04-02 | Mcdermott Technology Inc. | Compact, high-efficiency, gas/liquid separator method and apparatus |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1011045A (en) | 1963-01-24 | 1965-11-24 | Normalair Ltd | Improvements in or relating to air conditioning systems for aircraft |
US3852409A (en) * | 1972-10-31 | 1974-12-03 | Lone Star Steel Co | Process for the removal of particulate matter and acidic gases from carrier gases |
US3977810A (en) * | 1974-09-23 | 1976-08-31 | Kobe, Inc. | Multiple outlet, constant flow, pitot pump |
DE3519661A1 (en) * | 1985-06-01 | 1986-12-04 | M A N Technologie GmbH, 8000 München | METHOD AND DEVICE FOR SEPARATING CO (ARROW DOWN) 2 (ARROW DOWN) SHARES FROM GASES |
AU6021100A (en) | 1999-07-19 | 2001-02-05 | Ebara Corporation | Apparatus and method for cleaning acidic gas |
DE10054338C2 (en) | 2000-11-02 | 2003-11-27 | Antriebstechnik Katt Hessen Gm | Cooling system for low inertia rotating electrical machine |
-
2003
- 2003-06-30 US US10/611,490 patent/US7252703B2/en not_active Expired - Fee Related
-
2004
- 2004-06-29 WO PCT/US2004/020861 patent/WO2005005026A1/en active Application Filing
-
2007
- 2007-04-27 US US11/741,686 patent/US20080112869A1/en not_active Abandoned
Patent Citations (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3632519A (en) * | 1969-11-10 | 1972-01-04 | Us Navy | Aqueous solutions of omega-aminoalkyl alkylsulfones as regenerative co2 absorbents |
US3727375A (en) * | 1971-08-12 | 1973-04-17 | R Wallace | Continuous electromigration process for removal of gaseous contaminants from the atmosphere and apparatus |
US3969094A (en) * | 1973-12-11 | 1976-07-13 | E. I. Du Pont De Nemours And Company | Flue gas scrubber |
US4285918A (en) * | 1980-02-25 | 1981-08-25 | The United States Of America As Represented By The Secretary Of The Navy | Regenerative CO2 absorbent |
US4375975A (en) * | 1980-06-04 | 1983-03-08 | Mgi International Inc. | Centrifugal separator |
US4468234A (en) * | 1980-06-04 | 1984-08-28 | Mgi International, Inc. | Centrifugal separator |
US4810266A (en) * | 1988-02-25 | 1989-03-07 | Allied-Signal Inc. | Carbon dioxide removal using aminated carbon molecular sieves |
US5318758A (en) * | 1991-03-07 | 1994-06-07 | Mitsubishi Jukogyo Kabushiki Kaisha | Apparatus and process for removing carbon dioxide from combustion exhaust gas |
US6364940B1 (en) * | 1994-11-10 | 2002-04-02 | Mcdermott Technology Inc. | Compact, high-efficiency, gas/liquid separator method and apparatus |
US5876486A (en) * | 1995-09-09 | 1999-03-02 | Dornier Gmbh | Method and apparatus for removing carbon dioxide |
US6258215B1 (en) * | 1998-07-21 | 2001-07-10 | Otkrytoe aktsionernoe obschestvo “Nauchno-Issledovatelsky I Konstruktosky Institut Kkhimicheskogo Mashinostroenia (A. O. Neikhimmash”) | System and a rotary vacuum distiller for water recovery from aqueous solutions, preferably from urine aboard spacecraft |
US6132493A (en) * | 1998-08-05 | 2000-10-17 | Church; C. Daniel | Apparatus and method for washing air with a liquid without an eliminator |
US6190629B1 (en) * | 1999-04-16 | 2001-02-20 | Cbl Technologies, Inc. | Organic acid scrubber and methods |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7585476B2 (en) * | 2006-04-13 | 2009-09-08 | Babcock & Wilcox Power Generation Group Inc. | Process for controlling the moisture concentration of a combustion flue gas |
US20070243119A1 (en) * | 2006-04-13 | 2007-10-18 | William Downs | Process for controlling the moisture concentration of a combustion flue gas |
US8506693B2 (en) * | 2009-12-03 | 2013-08-13 | Mitsubishi Heavy Industries, Ltd | CO2 recovery system and CO2 recovery method |
US20110135550A1 (en) * | 2009-12-03 | 2011-06-09 | Mitsubishi Heavy Industries, Ltd. | Co2 recovery system and co2 recovery method |
US9238191B2 (en) | 2009-12-03 | 2016-01-19 | Mitsubishi Heavy Industries, Ltd. | CO2 recovery system and CO2 recovery method |
US8974582B2 (en) | 2009-12-25 | 2015-03-10 | Mitsubishi Heavy Industries, Ltd. | CO2 recovery system and CO2 recovery method |
US8398758B2 (en) * | 2009-12-25 | 2013-03-19 | Mitsubishi Heavy Industries, Ltd. | CO2 recovery system and CO2 recovery method |
US20110158891A1 (en) * | 2009-12-25 | 2011-06-30 | Mitsubishi Heavy Industries, Ltd. | Co2 recovery system and co2 recovery method |
RU2505341C1 (en) * | 2012-06-15 | 2014-01-27 | Общество с ограниченной ответственностью "НПО Пылеочистка" | Method of gas cleaning |
WO2013187802A3 (en) * | 2012-06-15 | 2014-03-27 | Khamidullin Rafik Nailovich | Gas purification method |
CN104540574A (en) * | 2012-06-15 | 2015-04-22 | 拉菲克·奈尔洛维奇·哈密杜林 | Gas purification method |
CN103920396A (en) * | 2014-03-31 | 2014-07-16 | 煤科集团杭州环保研究院有限公司 | Automatic open-type double-alkali-method desulphurized gypsum oxidation system and control method thereof |
CN103920396B (en) * | 2014-03-31 | 2015-11-25 | 煤科集团杭州环保研究院有限公司 | A kind of open type double alkali method desulfurizing gypsum autoxidation system and control method thereof |
CN109420407A (en) * | 2017-08-31 | 2019-03-05 | 双叶产业株式会社 | The method of carbon dioxide contained in carbon dioxide application equipment and recycling burning waste gas |
US11852062B2 (en) * | 2020-10-13 | 2023-12-26 | Daewoo Shipbuilding & Marine Engineering Co., Ltd. | Apparatus for reducing greenhouse gas emission in vessel and vessel including the same |
Also Published As
Publication number | Publication date |
---|---|
US20040265199A1 (en) | 2004-12-30 |
WO2005005026A1 (en) | 2005-01-20 |
US7252703B2 (en) | 2007-08-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US20080112869A1 (en) | Direct contact liquid air contaminant control system | |
US7306654B2 (en) | Method and apparatus for recovering water from atmospheric air | |
CN106731483A (en) | It is suitable for the exhaust treatment system of high humility organic exhaust gas | |
JP2002058952A (en) | Circulated gas-concentration method for recovered gas in dry-type dehumidifier | |
CN107569973A (en) | The absorption processing method and system of VOC organic exhaust gas | |
CN206587570U (en) | It is suitable for the exhaust treatment system of high humility organic exhaust gas | |
JP2011031159A (en) | Organic solvent recovery system | |
US6364943B1 (en) | Gas treatment system | |
US2129299A (en) | Recovery of solvents from gases | |
JP2014000526A (en) | Solvent recovery apparatus and method of controlling the same | |
JP2013132582A (en) | Organic solvent-containing gas treatment system | |
CN114867543A (en) | Organic solvent recovery system | |
JP5628051B2 (en) | Solvent recovery system | |
JPH10118440A (en) | Treatment of gas containing methanol | |
JP2002186821A (en) | Organic solvent vapor treatment apparatus | |
US20220355239A1 (en) | A volatile organic compound reduction apparatus | |
CN111790244A (en) | Organic gas treatment system and method | |
WO2005072850A1 (en) | Method and apparatus for recovering water from atmospheric air | |
JP3922449B2 (en) | Organic solvent recovery system | |
JP2567300B2 (en) | Solvent recovery equipment using dry air | |
CN110590633A (en) | Combined type NMP recovery system | |
JP3021092B2 (en) | Solvent recovery method | |
JPH06312117A (en) | Solvent recovery | |
JP7435367B2 (en) | Organic solvent recovery system | |
CN220214442U (en) | DMCA condensation recovery system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: HONEYWELL INTERNATIONAL INC., NEW JERSEY Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:MACKNIGHT, ALLEN K.;REEL/FRAME:019223/0824 Effective date: 20070425 |
|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |