US3905773A - System for supplying inert gas - Google Patents

System for supplying inert gas Download PDF

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US3905773A
US3905773A US318396A US31839672A US3905773A US 3905773 A US3905773 A US 3905773A US 318396 A US318396 A US 318396A US 31839672 A US31839672 A US 31839672A US 3905773 A US3905773 A US 3905773A
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exhaust
fuel
inert gas
gas
engine
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US318396A
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Walter G Brooks
John P Knodle
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Production Operators Inc
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Production Operators Inc
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/14Production of inert gas mixtures; Use of inert gases in general
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S48/00Gas: heating and illuminating
    • Y10S48/08Internal combustion engine for gas making

Definitions

  • Another object is to provide an improved system for insuring closer control of the catalytically converted gases in the exhaust system from an internal combustion engine.
  • the exhaust gases from an internal combustion engine are directed, as heretofore, through a catalytic converter.
  • an exhaust gas analyzer is utilized to control the BTU value of the fuel supply to the engine, by adding to the intake fuel controlled proportions of a gas having a substantially different BTU than the main fuel gas.
  • Greater BTU additive gas will be used where the fuel gas has an abnormally low BTU value (for example, less than about 900 BTU per cu. ft.) and lower BTU additive gas will be used where the fuel gas exceeds normal BTU values (for example, above 1000 BTU per cu. ft.).
  • For intermediate value fuel gas between about 900 and 1000 BTU per cu. ft.
  • either higher or lower BTU additive gas may be used with a corresponding adjustment of the carburetor or fuel mixing valves.
  • FIGURE is a schematic representation illustrating an exemplary form of the apparatus.
  • An internal combustion engine A preferably of the reciprocating type, is equipped with carburetion or mixing valve equipment B for properly mixing fuel and air constituents introduced through piping 6 and 7 for supply to the firing chambers.
  • the fuel supply may be natural gas which generally is present and available.
  • the exhaust line 8 leads from the engine exhaust manifold to a conventional catalytic converter C containing a suitable catalytic agent, such as platinum or palladium, over which the exhaust is directed for eliminating corrosive oxides of nitrogen and other undesirable materials.
  • the treated exhaust may then be supplied through line 10, valve 26, compressor E and line 9 to a process or consuming point, such as a water sweetening plant (for removal of gases such as H 8) or a subsurface oilproducing formation.
  • a process or consuming point such as a water sweetening plant (for removal of gases such as H 8) or a subsurface oilproducing formation.
  • the inert gas from the converter may be discharged to the atmosphere through line 10 and valve 25.
  • a portion of the exhaust is bypassed as at 1 1 to an exhaust gas analyzer D, also of conventional design, for instance, a thermal conductivity type.
  • the exhaust gas analyzer is adapted to respond to the chemical composition of the exhaust gas. Responses from the analyzer, delivered through a pneumatic or electrical line 12, energize the actuator 13 of an automatic valve 14 in a line 15 leading from a source of additive gas 16 to the main fuel supply line 6 and thence to the engine carburetion system.
  • the additive gas may be introduced into the intake manifold downstream of the carburetion system.
  • pneumatic line 12 may control an automatic valve 17 in a connection 18, shown dotted, between discharge duct 9 and line 15 and thence to the engine intake permitting a portion of the produced, essentially zero BTU inert gas to be used as the additive gas.
  • Manual valves 19 and 20 are provided in lines 15 and 18. In those embodiments where the exhaust is released to the atmosphere, the compressor E will be employed to raise the exhaust gas pressure only enough to permit flow through connection 18 through line 15 to intake line 6.
  • the purpose of the additive supplied, either through line 15, 6 or line 18, 15, 6 is to adjust the BTU value of the engine intake mixture so that the components of the exhaust in duct 8 will be optimum for action of the catalytic converter as explained above.
  • fuel gas has an intermediate BTU value (about 900 to 1000 BTU per cu. ft.) a lower BTU additive gas may be used and when the fuel gas has a high BTU value (above about 1000 BTU per cu. ft.) the additive gas should be an inert gas or a gas with a lower BTU value than that of the main supply gas.
  • the carburetor is initially adjusted without the additive gas to provide a rich fuel mixture so as to produce an excess of combustible gases as carbon monoxide and hydrogen in the exhaust over the amount required for efficient operation of the catalytic converter (about 24%).
  • the amount of excess caarbon monoxide and hydrogen in the exhaust before the introduction of the additive is not critical but it should be sufficiently in excess of the desired amount to be certain that a sufficient amount will always be available with normal fluctuations in the BTU value of the fuel supply.
  • Inert or low BTU gas additives may be supplied from the additive gas source 16 through manual valve 19 and past the automatic control valve 14.
  • the additive gas source 16 may be supplied from the additive gas source 16 through manual valve 19 and past the automatic control valve 14.
  • the catalytic converter When inert gas issupplied to a consuming point or process, the alternate supply of inert gas may be obtained by opening manual valve and the inert gas will then be supplied tothe fuel system through automatic control valve 17. Manual valves 19 and will be closed at this time.
  • Valve 26 is provided to illustrate an embodiment in which compressor E would not be used and the entire production of inert gas would be discharged through manual valve 25 to the atmosphere. Such circumstance would normally occur when the catalytic converter is used to reduce the undesirable corrosive or combustible components of the exhaust gas for discharge to the atmosphere and the source 16 is used for the additive gas supply.
  • Source 16 may be used to store a supply of gas of lesser or greater BTU value than the main gas supply.
  • a gas having a greater BTU value than that of normally available natural gas would include, for example, an LPG (liquified petroleum gas) such as butane or propane.
  • LPG liquid petroleum gas
  • Such a high BTU gas may be used if the fuel gas has an intermediate BTU value (about 900-1000 BTU per cu. ft.) and such greater BTU additive will be used if the fuel gas has a relatively low BTU value (below about 900 BTU per cu. ft.).
  • the carburetor or fuel mixing valve will be adjusted to a lean mixture as evidenced by a low proportion of combustibles in the exhaust gas, normally less than 2 percent, before the additive is introduced into the fuel supply.
  • the rich additive gas is then introduced as in the case of the lean additive gas by opening manual valve 19 and controlling the desired proportion supplied to the carburetor system by the operation of automatic valve 14.
  • Exhaust gas analyzing means connected to said duct means between said engine and said converter to sample and respond to the chemical composition of the exhaust gas
  • Inert gas generating apparatus as described in claim 1 in which said source of fuel additive is adapted to supply to the engine a fuel additive comprising a liquefied petroleum gas of greater BTU value than the BTU value of the gas delivered by said fuel supply means.
  • Inert gas generating apparatus as described in claim 1 in which said source of fuel additive comprises a communication with said exhaust duct downstream of the catalytic converter.
  • Inert gas generating apparatus as described in claim 1 wherein a compressor is connected to said exhaust duct downstream from said converter, and a discharge conduit is connected to said compressor to carry said inert gas from said compressor to a consuming point.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Biomedical Technology (AREA)
  • Health & Medical Sciences (AREA)
  • Organic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Electrical Control Of Air Or Fuel Supplied To Internal-Combustion Engine (AREA)
  • Output Control And Ontrol Of Special Type Engine (AREA)
  • Exhaust Gas After Treatment (AREA)

Abstract

The exhaust gases from an internal combustion engine are processed for release to the atmosphere or for delivery to a consuming point, such as a subsurface oil producing formation, by passage through a catalytic converter which reduces or eliminates corrosive, combustible, and other undesirable components of the exhaust. In order to insure the presence in the gases of optimum chemical components for effecting the catalytic reaction, an exhaust analyzer and controller adjusts the supply to the engine of an additive of different BTU value than the main fuel supply.

Description

United States Patent Brooks et al.
[451 Sept. 16, 1975 r SYSTEM FOR SUPPLYING INERT GAS lnventors: Walter G. Brooks, Houston, Tex.;
John P. Knodle, Ventura, Calif.
[73] Assignee:
Production Operators, Inc.,
Houston, Tex.
Filed:
US. Cl.
Int. Cl.
Dec. 26, 1972 Appl. No.: 318,396
BOIJ 7/00; F01N 3/15 Field of Search 23/288 F, 281; 123/121;
60/276, 285; 48/DlG. 8
References Cited UNITED STATES PATENTS 48/D1G. 8 123/121 X Barstow 23/281 UX Barlow 23/288 F X Keith et a1. 60/276 X Barstow 60/276 X Burridge 73/116 Urquhart Rockwell 3,696,618 10/1972 Boyd et al. 23/288 F X 3,718,000 2/1973 60/285 3,725,012 4/1973 23/288 F X 3,753,424 8/1973 123/121 3,800,768 4/1974 Rhodes et a1. 60/285 X Primary ExaminerJoseph Scovronek Assistant ExaminerArnold Turk Attorney, Agent, or Firm-Delmar L. Sroufe; Frank B. Pugsley; Larry B. Feldcamp [57] ABSTRACT 5 Claims, 1 Drawing Figure SYSTEM FOR SUPPLYING INERT GAS BACKGROUND OF THE lNVENTiQN Where the exhaust from an internal combustion engine is to be utilized as an inert gas, for instance, supplied through a compressor to a subsurface oil producing formation, it is necessary torender the exhaust essentially free of corrosive, acid-forming and other undesirable components. This has been achieved heretofore by installing in the exhaust duct a catalytic converter containing a catalyst such as platinum or palla-' dium which induces a reduction of the nitrogen oxides and elimination of free oxygen. However, the efficacy of such a converter depends upon the presence in the exhaust of optimum quantities of reducing agents such as carbon monoxide and free hydrogen. The prior art devices for insuring the optimum chemical composition of the exhaust gases for such catalytic conversion have utilized exhaust gas ahalyzers either to adjust the ratio of fuel and air in the combustible mixture supplied to the engine, or have supplied an additive, as the fuel itself, directly to the catalytic converter. In the first case, proper control of the combustible content of exhaust gases by control of the fuel and air ratio in the mixture supplied to multiple carburetors or mixing valves is not feasible. In the latter case, close control of the exhaust constituents has not been achieved.
Accordingly, it is an object of the present invention to provide a system for rendering the exhaust gases from an internal combustion engine continuously at the optimum composition for maximum catalytic conversion even where multiple carburetors are used.
Another object is to provide an improved system for insuring closer control of the catalytically converted gases in the exhaust system from an internal combustion engine.
SUMMARY OF THE INVENTION In accordance with the present invention the exhaust gases from an internal combustion engine are directed, as heretofore, through a catalytic converter. In order to improve the converter action, an exhaust gas analyzer is utilized to control the BTU value of the fuel supply to the engine, by adding to the intake fuel controlled proportions of a gas having a substantially different BTU than the main fuel gas. Greater BTU additive gas will be used where the fuel gas has an abnormally low BTU value (for example, less than about 900 BTU per cu. ft.) and lower BTU additive gas will be used where the fuel gas exceeds normal BTU values (for example, above 1000 BTU per cu. ft.). For intermediate value fuel gas (between about 900 and 1000 BTU per cu. ft.) either higher or lower BTU additive gas may be used with a corresponding adjustment of the carburetor or fuel mixing valves.
In the accompanying drawing, the FIGURE is a schematic representation illustrating an exemplary form of the apparatus.
DETAILED DESCRIPTION OF THE FIGURE An internal combustion engine A, preferably of the reciprocating type, is equipped with carburetion or mixing valve equipment B for properly mixing fuel and air constituents introduced through piping 6 and 7 for supply to the firing chambers. Where the apparatus is utilized in the oilfields, the fuel supply may be natural gas which generally is present and available. The exhaust line 8leads from the engine exhaust manifold to a conventional catalytic converter C containing a suitable catalytic agent, such as platinum or palladium, over which the exhaust is directed for eliminating corrosive oxides of nitrogen and other undesirable materials. The treated exhaust may then be supplied through line 10, valve 26, compressor E and line 9 to a process or consuming point, such as a water sweetening plant (for removal of gases such as H 8) or a subsurface oilproducing formation. Alternatively, the inert gas from the converter may be discharged to the atmosphere through line 10 and valve 25.
A portion of the exhaust is bypassed as at 1 1 to an exhaust gas analyzer D, also of conventional design, for instance, a thermal conductivity type. The exhaust gas analyzer is adapted to respond to the chemical composition of the exhaust gas. Responses from the analyzer, delivered through a pneumatic or electrical line 12, energize the actuator 13 of an automatic valve 14 in a line 15 leading from a source of additive gas 16 to the main fuel supply line 6 and thence to the engine carburetion system. Alternatively, the additive gas may be introduced into the intake manifold downstream of the carburetion system.
As another alternative, pneumatic line 12 may control an automatic valve 17 in a connection 18, shown dotted, between discharge duct 9 and line 15 and thence to the engine intake permitting a portion of the produced, essentially zero BTU inert gas to be used as the additive gas. Manual valves 19 and 20 are provided in lines 15 and 18. In those embodiments where the exhaust is released to the atmosphere, the compressor E will be employed to raise the exhaust gas pressure only enough to permit flow through connection 18 through line 15 to intake line 6.
OPERATION The purpose of the additive supplied, either through line 15, 6 or line 18, 15, 6 is to adjust the BTU value of the engine intake mixture so that the components of the exhaust in duct 8 will be optimum for action of the catalytic converter as explained above. Where fuel gas has an intermediate BTU value (about 900 to 1000 BTU per cu. ft.) a lower BTU additive gas may be used and when the fuel gas has a high BTU value (above about 1000 BTU per cu. ft.) the additive gas should be an inert gas or a gas with a lower BTU value than that of the main supply gas. With the use of such low BTU or inert additive gas, the carburetor is initially adjusted without the additive gas to provide a rich fuel mixture so as to produce an excess of combustible gases as carbon monoxide and hydrogen in the exhaust over the amount required for efficient operation of the catalytic converter (about 24%). The amount of excess caarbon monoxide and hydrogen in the exhaust before the introduction of the additive is not critical but it should be sufficiently in excess of the desired amount to be certain that a sufficient amount will always be available with normal fluctuations in the BTU value of the fuel supply.
Inert or low BTU gas additives may be supplied from the additive gas source 16 through manual valve 19 and past the automatic control valve 14. In the alternative,
the catalytic converter. When inert gas issupplied to a consuming point or process, the alternate supply of inert gas may be obtained by opening manual valve and the inert gas will then be supplied tothe fuel system through automatic control valve 17. Manual valves 19 and will be closed at this time.
When the produced inert gas is used as an alternate supply of fuel additive gas and the remainder of the produced inert gas is discharged to the atmosphere, manual valves 20 and 25 will be open and valves 19 and 27 will be closed. As previously noted, in this case the compressor E will then be employed only to raise the exhaust gas pressure sufficiently to permit flow through line 18, valve 20 andline 15 to the engine intake 6. During such operation automatic control valve 17 will control the supply of the inert gas to the fuel mixture.
Valve 26 is provided to illustrate an embodiment in which compressor E would not be used and the entire production of inert gas would be discharged through manual valve 25 to the atmosphere. Such circumstance would normally occur when the catalytic converter is used to reduce the undesirable corrosive or combustible components of the exhaust gas for discharge to the atmosphere and the source 16 is used for the additive gas supply.
Source 16 may be used to store a supply of gas of lesser or greater BTU value than the main gas supply. A gas having a greater BTU value than that of normally available natural gas would include, for example, an LPG (liquified petroleum gas) such as butane or propane. Such a high BTU gas may be used if the fuel gas has an intermediate BTU value (about 900-1000 BTU per cu. ft.) and such greater BTU additive will be used if the fuel gas has a relatively low BTU value (below about 900 BTU per cu. ft.). In such case, of course, the carburetor or fuel mixing valve will be adjusted to a lean mixture as evidenced by a low proportion of combustibles in the exhaust gas, normally less than 2 percent, before the additive is introduced into the fuel supply. The rich additive gas is then introduced as in the case of the lean additive gas by opening manual valve 19 and controlling the desired proportion supplied to the carburetor system by the operation of automatic valve 14.
We have found that the system herein disclosed and claimed insures the supply of an exceptionally uniform composition of exhaust gases, particularly as to reductants, to the catalytic converter, with the result that the main fuel gas supply may be controlled as necessary for proper engine operation and also for continuing uniform supply of inert gas to the consuming point. Various features may be modified as will occur to those skilled in the art, and the exclusive use of all modifications as come within the scope of the appended claims is contemplated.
We claim:
1. In an apparatus for the production of an inert gas by the conversion of exhaust gas from an internal combustion engine said apparatus having a source of hydrocarbon fuel of predetermined BTU value connected to said engine by a fuel supply means, and exhaust duct means connected to said engine to convey the exhaust gases therefrom; and a catalytic converter provided in said duct means for reacting the exhaust gases over a catalyst of the group consisting of platinum and palladium, the improvement comprising:
a. Exhaust gas analyzing means connected to said duct means between said engine and said converter to sample and respond to the chemical composition of the exhaust gas;
b. A source of fuel additive of BTU value differing from that of the hydrocarbon fuel;
c. A connection between said latter source of fuel additive and said fuel supply means;
d. A valve controlling said connection; and
e. An operative connection between said analyzing means and said valve for adjusting the quantity of fuel additive admixed with said hydrocarbon fuel supplied to the engine in proportions which will maintain the combustibles in the exhaust gas at a level sufficient for efficient operation of the catalytic converter.
2. Inert gas generating apparatus as described in claim 1 in which said source of fuel additive is adapted to supply to the engine a fuel additive comprising a liquefied petroleum gas of greater BTU value than the BTU value of the gas delivered by said fuel supply means.
3. Inert gas generating apparatus as described in claim 1 in which said source of fuel additive comprises a communication with said exhaust duct downstream of the catalytic converter.
4. Inert gas generating apparatus as described in claim 1 wherein a compressor is connected to said exhaust duct downstream from said converter, and a discharge conduit is connected to said compressor to carry said inert gas from said compressor to a consuming point.
5. Inert gas generating apparatus as described in claim 1 wherein a discharge conduit is connected to said catalytic converter to release said inert gas to the atmosphere.

Claims (5)

1. IN AN APPARATUS FOR THE PRODUCTION OF AN INERT GAS BY THE CONVERSION OF EXHAUST GAS FROM AN INTERNL COMBUSTION ENGINE SAID APPARATUS HAVING A SOURCE OF HYDROCARBON FUEL OF PREDETERMINED BTU VALUE CONNECTED TO SAID ENGINE BY A FUEL SUPPLY MEANS, AND EXHAUST DUCT MEANS CONNECTED TO SAID ENGINE TO CONVEY THE EXHAUST GASES THEREFROM, AND A CATALYTIC CONVERTER PROVIDED IN SAID DUCT MEANS FOR REACTING THE EXHAUST GASES OVER A CATALYST OF THE GROUP CONSISTING OF PLATINUM AND PALLADIUM, THE IMPROVEMENT COMPRISING: A. EXHAUST GAS ANALYZING MEANS CONNECTED TO SAID DUCT MEANS BETWEEN SAID ENGINE AND SAID CONVERTER TO SAMPLE AND RESPOND TO THE CHEMICAL COMPOSITION OF THE EXHAUST GAS, B. A SOURCE OF FUEL ADDITIVE OF BTU VALUE DIFFERING FROM THAT OF THE HYDROCARBON FUEL, C. A CONNECTION BETWEEN SAID LATTER SOURCE OF FUEL ADDITIVE AND SAID FUEL SUPPLY MEANS, D. A VALVE CONTROLLING SAID CONNECTION, AND E. AN OPERATIVE CONNECTION BETWEEN SAID ANALYZING MEANS AND SAID VALVE FOR ADJUSTING THE QUANTITY OF FUEOL ADDITIVE ADMIXED WITH SAID HYDROCARBON FUEL SUPPLIED TO THE ENGINE IN PROPORTIONS WHICH WILL MAINTAIN THE COMBUSTIBLES
2. Inert gas generating apparatus as described in claim 1 in which said source of fuel additive is adapted to supply to the engine a fuel additive comprising a liquefied petroleum gas of greater BTU value than the BTU value of the gas delivered by said fuel supply means.
3. Inert gas generating apparatus as described in claim 1 in which said source of fuel additive comprises a communication with said exhaust duct downstream of the catalytic converter.
4. Inert gas generating apparatus as described in claim 1 wherein a compressor is connected to said exhaust duct downstream from said converter, and a discharge conduit is connected to said compressor to carry said inert gas from said compressor to a consuming point.
5. Inert gas generating apparatus as described in claim 1 wherein a discharge conduit is connected to said catalytic converter to release said inert gas to the atmosphere.
US318396A 1972-12-26 1972-12-26 System for supplying inert gas Expired - Lifetime US3905773A (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3957418A (en) * 1974-05-09 1976-05-18 Naoyasu Sata Method and an apparatus for performing closed combustion
US3963011A (en) * 1973-07-26 1976-06-15 Nissan Motor Co., Ltd. Method and device for adjusting engine exhaust gas recirculation control
US4440137A (en) * 1982-07-12 1984-04-03 Propane Carburetion Systems, Inc. Supplemental fuel supply device for I.C. engine
GB2265555A (en) * 1992-04-01 1993-10-06 Petroleo Brasileiro Sa Mounted system for inert gas generation
US5456064A (en) * 1994-06-23 1995-10-10 Inert Gas Services Inc. Method and apparatus for producing an inert gas
US20050115404A1 (en) * 2003-12-02 2005-06-02 Honeywell International Inc. Gas generating system and method for inerting aircraft fuel tanks

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2363708A (en) * 1941-02-28 1944-11-28 Kenneth M Urquhart Gas producer system
US2785966A (en) * 1948-10-02 1957-03-19 Edward A Rockwell Carburetor for internal combustion engines
US3000707A (en) * 1959-05-29 1961-09-19 Southwest Ind Inc Process for generating inert gas
US3224188A (en) * 1964-04-10 1965-12-21 Joseph S Barlow Combustion control
US3441381A (en) * 1965-06-22 1969-04-29 Engelhard Ind Inc Apparatus for purifying exhaust gases of an internal combustion engine
US3464801A (en) * 1964-09-28 1969-09-02 Tenex Corp The Catalytic system for inert gas generation
US3554021A (en) * 1969-06-30 1971-01-12 Sylvania Electric Prod Portable test equipment with extendable display means
US3696618A (en) * 1971-04-19 1972-10-10 Universal Oil Prod Co Control system for an engine system
US3718000A (en) * 1971-06-01 1973-02-27 B Walker Dual fueled engine with temperature switchover
US3725012A (en) * 1971-01-27 1973-04-03 G Gower Apparatus for manufacturing high pressure inert gas
US3753424A (en) * 1970-12-22 1973-08-21 Steyr Daimler Puch Ag Method and apparatus for supplying gaseous and liquid fuels to a dual-fuel engine
US3800768A (en) * 1972-02-28 1974-04-02 Standard Oil Co Apparatus and method for fueling an internal combustion engine

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2363708A (en) * 1941-02-28 1944-11-28 Kenneth M Urquhart Gas producer system
US2785966A (en) * 1948-10-02 1957-03-19 Edward A Rockwell Carburetor for internal combustion engines
US3000707A (en) * 1959-05-29 1961-09-19 Southwest Ind Inc Process for generating inert gas
US3224188A (en) * 1964-04-10 1965-12-21 Joseph S Barlow Combustion control
US3464801A (en) * 1964-09-28 1969-09-02 Tenex Corp The Catalytic system for inert gas generation
US3441381A (en) * 1965-06-22 1969-04-29 Engelhard Ind Inc Apparatus for purifying exhaust gases of an internal combustion engine
US3554021A (en) * 1969-06-30 1971-01-12 Sylvania Electric Prod Portable test equipment with extendable display means
US3753424A (en) * 1970-12-22 1973-08-21 Steyr Daimler Puch Ag Method and apparatus for supplying gaseous and liquid fuels to a dual-fuel engine
US3725012A (en) * 1971-01-27 1973-04-03 G Gower Apparatus for manufacturing high pressure inert gas
US3696618A (en) * 1971-04-19 1972-10-10 Universal Oil Prod Co Control system for an engine system
US3718000A (en) * 1971-06-01 1973-02-27 B Walker Dual fueled engine with temperature switchover
US3800768A (en) * 1972-02-28 1974-04-02 Standard Oil Co Apparatus and method for fueling an internal combustion engine

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3963011A (en) * 1973-07-26 1976-06-15 Nissan Motor Co., Ltd. Method and device for adjusting engine exhaust gas recirculation control
US3957418A (en) * 1974-05-09 1976-05-18 Naoyasu Sata Method and an apparatus for performing closed combustion
US4440137A (en) * 1982-07-12 1984-04-03 Propane Carburetion Systems, Inc. Supplemental fuel supply device for I.C. engine
GB2265555A (en) * 1992-04-01 1993-10-06 Petroleo Brasileiro Sa Mounted system for inert gas generation
GB2265555B (en) * 1992-04-01 1995-11-15 Petroleo Brasileiro Sa Process and apparatus for inert gas generation
US5456064A (en) * 1994-06-23 1995-10-10 Inert Gas Services Inc. Method and apparatus for producing an inert gas
US20050115404A1 (en) * 2003-12-02 2005-06-02 Honeywell International Inc. Gas generating system and method for inerting aircraft fuel tanks
US7081153B2 (en) 2003-12-02 2006-07-25 Honeywell International Inc. Gas generating system and method for inerting aircraft fuel tanks
US20070000380A1 (en) * 2003-12-02 2007-01-04 Honeywell International Inc. Gas generating system and method for inerting aircraft fuel tanks
US7306644B2 (en) 2003-12-02 2007-12-11 Honeywell International, Inc. Gas generating system and method for inerting aircraft fuel tanks

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