US20050129599A1 - Ammonia storage and injection in NOx control - Google Patents

Ammonia storage and injection in NOx control Download PDF

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US20050129599A1
US20050129599A1 US11/046,042 US4604205A US2005129599A1 US 20050129599 A1 US20050129599 A1 US 20050129599A1 US 4604205 A US4604205 A US 4604205A US 2005129599 A1 US2005129599 A1 US 2005129599A1
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Prior art keywords
ammonia
water
container
mixture
engine
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US11/046,042
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Lester Berriman
John Zabsky
Lionel Simons
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KLEENAIR SYSTEMS INTERNATIONAL PLC
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KleenAir Systems Inc
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Priority to US11/046,042 priority Critical patent/US20050129599A1/en
Assigned to KLEENAIR SYSTEMS, INC. reassignment KLEENAIR SYSTEMS, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: SIMONS, LIONEL, BERRIMAN, LESTER P., ZABSKY, JOHN M.
Publication of US20050129599A1 publication Critical patent/US20050129599A1/en
Assigned to KLEENAIR SYSTEMS INTERNATIONAL PLC reassignment KLEENAIR SYSTEMS INTERNATIONAL PLC ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: KLEENAIR SYSTEMS, INC.
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
    • F01N3/18Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
    • F01N3/20Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
    • F01N3/2066Selective catalytic reduction [SCR]
    • 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
    • B01D53/46Removing components of defined structure
    • B01D53/54Nitrogen compounds
    • B01D53/56Nitrogen oxides
    • 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
    • B01D53/90Injecting reactants
    • 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
    • B01D53/92Chemical or biological purification of waste gases of engine exhaust gases
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/20Reductants
    • B01D2251/206Ammonium compounds
    • B01D2251/2062Ammonia
    • 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
    • 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
    • B01D53/92Chemical or biological purification of waste gases of engine exhaust gases
    • B01D53/94Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • B01D53/9404Removing only nitrogen compounds
    • B01D53/9409Nitrogen oxides
    • B01D53/9413Processes characterised by a specific catalyst
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2610/00Adding substances to exhaust gases
    • F01N2610/02Adding substances to exhaust gases the substance being ammonia or urea
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2610/00Adding substances to exhaust gases
    • F01N2610/06Adding substances to exhaust gases the substance being in the gaseous form
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2610/00Adding substances to exhaust gases
    • F01N2610/14Arrangements for the supply of substances, e.g. conduits
    • F01N2610/1453Sprayers or atomisers; Arrangement thereof in the exhaust apparatus
    • 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies

Definitions

  • ammonia Another way for storing ammonia is to store it as urea (H 2 NCO NH 2 ) as in a solution with water, and inject it into the exhaust gas stream.
  • urea H 2 NCO NH 2
  • ammonia Since the temperature of the exhaust gas stream very rapidly drops as the exhaust gasses move through the exhaust pipe into the atmosphere, it is desirable that the reactions occur very rapidly so they can occur at the high temperatures that exist in and near the exhaust gas manifold so that a high proportion of the injected material (ammonia or urea) can react with the nitrogen oxides.
  • a system for storing and injecting ammonia into the exhaust gasses of an engine, which enables safe storage of the ammonia and the injection of ammonia into the exhaust gasses for rapid reaction with nitrogen oxides.
  • the ammonia is stored as a liquid mixture of ammonia and water.
  • the ammonia is preferably stored as a mixture of between 30 and 70 grams of ammonia per 100 grams of water.
  • the liquid mixture is drawn off through a tube leading from the container. In one system, the tube is heated by the exhaust gasses and the mixture of ammonia and water is injected directly into the exhaust gasses.
  • FIG. 1 is a simplified schematic view of an engine, with pollution reduction apparatus of the present invention installed therein.
  • FIG. 2 is a graph showing variation of the saturation mass of ammonia in water as a function of temperature.
  • FIG. 3 is a graph similar to that of FIG. 2 , but showing variation of the saturation percent (by mass) of ammonia in a mixture of ammonia and water, as a function of temperature.
  • FIG. 4 is an enlarged view of a portion of the system of FIG. 1 , showing separation of a liquid mixture of ammonia and water into gaseous ammonia and water vapor.
  • FIG. 5 is a sectional-view showing a portion of the apparatus of FIG. 2 .
  • FIG. 6 is a simplified schematic view of a system of another embodiment of the invention.
  • FIG. 1 illustrates a system 10 of the present invention, wherein an engine 12 has cylinders in which fuel and air are combusted to turn a crankshaft 14 .
  • the combustion produces hot exhaust gasses that are passed through an exhaust conduit 16 into the atmosphere.
  • the exhaust conduit includes a manifold 20 that is connected to a few cylinders to collect the exhaust gasses therefrom.
  • a catalytic convertor 22 that lies along the exhaust conduit, is widely used in vehicle engines to reduce pollution.
  • FIG. 1 shows an ammonia injection system 30 that includes a source 32 of ammonia.
  • An injector apparatus 33 includes a metering valve 34 , tube 36 with tube portion 62 , and an injection nozzle at 40 .
  • the metering valve 34 passes ammonia from the source through a tube 36 to an ammonia injection location 40 where ammonia is injected into the exhaust conduit 16 to mix with hot exhaust gasses.
  • the location 40 lies in or close to the exhaust gas manifold 20 , so the ammonia encounters very hot exhaust gasses (usually over 1100° F. at high engine loads) to promote the reaction of ammonia and the exhaust gasses and thereby reduce nitrogen oxides.
  • the source 32 for ammonia is a container 50 that contains a mixture 70 of ammonia in water.
  • FIG. 2 includes a graph 52 showing the mass of ammonia, at saturation in a solution that contains 100 grams of water, at different temperatures.
  • FIG. 3 contains a similar graph 54 that shows the saturation percent, by mass, of ammonia in a solution of ammonia and water. It can be seen that the percent ammonia (by mass), ranges from about 47% at 32° F. through 33% ammonia at 72° F., down to 0% at 212° F.
  • the container is kept away from the engine and is cooled by air, to avoid heating the container. If the container should be heated so that gaseous ammonia begins to accumulate under pressure and the pressure exceeds a certain limit (e.g. 2 psi), a relief valve 60 ( FIG. 1 ) will slowly vent the gaseous ammonia into the atmosphere. The rate of ammonia vented is very small, so it is not dangerous.
  • a check valve 61 ( FIG. 1 ) can admit air to avoid a vacuum above the liquid when the liquid is withdrawn.
  • the tube 36 that carries the ammonia-water mixture has a portion 62 that is wrapped about the exhaust conduit 16 , to rapidly heat the ammonia-water mixture that passes through the tube 36 to the injection location 40 .
  • FIG. 4 indicates how the ammonia may be separated from the water at a separation station 68 , before injection of the ammonia into the exhaust conduit.
  • the mixture 70 at a temperature such as 75° F. passes through the tube 36 , to the tube portion 62 that is in a heat-exchange relationship with the exhaust conduit, so material within the tube portion 62 is rapidly heated.
  • the initial percent of ammonia being about 25%, the ammonia is not released as a gas until the mixture reaches the location 72 which is at about 105° F. Progressively more ammonia is released as the temperature of the mixture progressively increases.
  • the mixture has a temperature of about 200° F., and only a few percent of ammonia remains in the mixture.
  • the rest of the ammonia continues along a tube end portion 82 , that carries the ammonia along a path 83 to an injector shown at 84 in FIG. 4 .
  • the injector can be of the type described in our earlier U.S. Pat. No. 5,992,141, which results in rapid heating of the gaseous ammonia prior to its injection into the very high temperature exhaust gasses, to activate the ammonia (break down some of the ammonia into its constituents) for injection into the exhaust gas stream.
  • the liquid 90 shown in FIG. 4 which moves along a path 91 , contains only a very small percent of ammonia, and is disposed of.
  • One way to dispose of it, indicated in FIG. 1 is to carry the liquid with a very small percent of ammonia along a tube 92 for injection at 94 into the exhaust pipe.
  • the location 94 is a location where the temperature of the exhaust gasses have been reduced to perhaps 250° F., in which case the small quantity of injected water will evaporate and become part of the exhaust gas stream that is admitted into the atmosphere.
  • small pumps may be located in the injection system 30 where pressure increases are required. In FIG.
  • the metering valve 34 is controlled by a circuit 100 that also controls a fuel injector 102 that injects fuel from a fuel line 104 into the engine cylinders. As discussed in my earlier U.S. Pat. No. 5,992,141, this varies the amount of ammonia in accordance with the load on the engine, to more effectively neutralize nitrogen oxides.
  • FIG. 6 illustrates a system 110 which includes a container 112 that contains the mixture 70 of ammonia (NH 3 ) and water (HO 2 ). Other ingredients can be added to the mixture 70 , but applicant prefers that most of the mixture be water and ammonia.
  • the ammonia is required to reduce nitrogen oxides and the water is useful to retain the ammonia and is a liquid that is easily disposed of because of its benign characteristics.
  • applicant passes the mixture 70 , which may have perhaps 25% ammonia by weight, and water, directly through a nozzle 84 that lies in the exhaust gas conduits 16 , at an upstream location near or in the exhaust manifold.
  • This system has the disadvantage that water is injected with the ammonia into the hot exhaust gasses, and tends to cool the exhaust gasses more rapidly. However, the amount of water and ammonia is very small, so the cooling effect of the water is very small.
  • This system also has the disadvantage that the ammonia is heated only moderately by the hot nozzle prior to injection into the exhaust gas stream, so only a low percent of the ammonia is activated to break down the ammonia into its components (NH 2 and NH) prior to injection.
  • the simplicity of the system 110 can make it useful even if its effectiveness in reducing nitrogen oxides is not as great.
  • the invention provides a system for reducing nitrogen oxides in the exhaust gasses of an engine by the injection of ammonia into the exhaust gasses, which facilitates storage of the ammonia.
  • the ammonia is stored as a mixture of ammonia and water (other liquids can be present), with the percent of ammonia preferably being between about 15% and 50% to avoid the generation of pressured ammonia gas.
  • the mixture is heated to convert most of the ammonia into its gaseous state and separate it from the water that still remains liquid, and with the gaseous ammonia being further heated to activate at least a portion of it and then being injected into the hot exhaust gasses near or in the exhaust gas manifold.
  • the ammonia and water mixture 15 flowed towards the exhaust gas conduit and both ammonia and water are injected into the exhaust conduit.

Abstract

A system is described for storing ammonia and injecting it into the exhaust gas stream of an engine to reduce nitrogen oxides. The ammonia is stored as a liquid mixture (70) of ammonia and water in a container (50). In one system, the mixture passes through a hot nozzle and is injected into an upstream portion of the exhaust gas pipe.

Description

    CROSS-REFERENCE
  • This is a continuation-in-part of Ser. No. 10/132,552 filed Apr. 24, 2002.
  • BACKGROUND OF THE INVENTION
  • In our earlier U.S. Pat. Nos. 5,224,346 and 5,992,141, we described experiments which showed that the amount of nitrogen oxides (NO and NO2), or NOx in engine exhaust gasses can be reduced by injecting ammonia (NH3) which reacts with nitrogen oxides to produce nitrogen and water. One practical problem is how to store ammonia that is to be injected into the exhaust gas stream. Ammonia can be stored as a liquid, at a pressure of about 150 psi, with the ammonia turning into gas when removed from the container and its pressure reduced. It is often undesirable to store ammonia under considerable pressure because of the danger of an explosion and the possibility of rapid leakage of ammonia. Another way for storing ammonia is to store it as urea (H2 NCO NH2) as in a solution with water, and inject it into the exhaust gas stream. However, it can take a longer time for urea to react with nitrogen oxides and turn them into nitrogen and water, than ammonia. Since the temperature of the exhaust gas stream very rapidly drops as the exhaust gasses move through the exhaust pipe into the atmosphere, it is desirable that the reactions occur very rapidly so they can occur at the high temperatures that exist in and near the exhaust gas manifold so that a high proportion of the injected material (ammonia or urea) can react with the nitrogen oxides. A system that enabled the storage of ammonia (NH3) without requiring storage under high pressure, so that the ammonia could be directly injected into hot exhaust gasses and rapidly react with nitrogen oxides, would be of value.
  • SUMMARY OF THE INVENTION
  • In accordance with one embodiment of the present invention, a system is provided for storing and injecting ammonia into the exhaust gasses of an engine, which enables safe storage of the ammonia and the injection of ammonia into the exhaust gasses for rapid reaction with nitrogen oxides. The ammonia is stored as a liquid mixture of ammonia and water. The ammonia is preferably stored as a mixture of between 30 and 70 grams of ammonia per 100 grams of water. The liquid mixture is drawn off through a tube leading from the container. In one system, the tube is heated by the exhaust gasses and the mixture of ammonia and water is injected directly into the exhaust gasses.
  • The novel features of the invention are set forth with particularity in the appended claims. The invention will be best understood from the following description when read in conjunction with the accompanying drawings.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • FIG. 1 is a simplified schematic view of an engine, with pollution reduction apparatus of the present invention installed therein.
  • FIG. 2 is a graph showing variation of the saturation mass of ammonia in water as a function of temperature.
  • FIG. 3 is a graph similar to that of FIG. 2, but showing variation of the saturation percent (by mass) of ammonia in a mixture of ammonia and water, as a function of temperature.
  • FIG. 4 is an enlarged view of a portion of the system of FIG. 1, showing separation of a liquid mixture of ammonia and water into gaseous ammonia and water vapor.
  • FIG. 5 is a sectional-view showing a portion of the apparatus of FIG. 2.
  • FIG. 6 is a simplified schematic view of a system of another embodiment of the invention.
  • DESCRIPTION OF THE PREFERRED EMBODIMENTS
  • FIG. 1 illustrates a system 10 of the present invention, wherein an engine 12 has cylinders in which fuel and air are combusted to turn a crankshaft 14. The combustion produces hot exhaust gasses that are passed through an exhaust conduit 16 into the atmosphere. The exhaust conduit includes a manifold 20 that is connected to a few cylinders to collect the exhaust gasses therefrom. A catalytic convertor 22 that lies along the exhaust conduit, is widely used in vehicle engines to reduce pollution.
  • FIG. 1 shows an ammonia injection system 30 that includes a source 32 of ammonia. An injector apparatus 33 includes a metering valve 34, tube 36 with tube portion 62, and an injection nozzle at 40. The metering valve 34 passes ammonia from the source through a tube 36 to an ammonia injection location 40 where ammonia is injected into the exhaust conduit 16 to mix with hot exhaust gasses. The location 40 lies in or close to the exhaust gas manifold 20, so the ammonia encounters very hot exhaust gasses (usually over 1100° F. at high engine loads) to promote the reaction of ammonia and the exhaust gasses and thereby reduce nitrogen oxides.
  • In accordance with the present invention, the source 32 for ammonia is a container 50 that contains a mixture 70 of ammonia in water. FIG. 2 includes a graph 52 showing the mass of ammonia, at saturation in a solution that contains 100 grams of water, at different temperatures. FIG. 3 contains a similar graph 54 that shows the saturation percent, by mass, of ammonia in a solution of ammonia and water. It can be seen that the percent ammonia (by mass), ranges from about 47% at 32° F. through 33% ammonia at 72° F., down to 0% at 212° F. As a practical matter, applicant can vary the percent ammonia according to the weather, but prefers to establish about 25% ammonia, so the ammonia will not go out of the mixture unless the temperature of the mixture increases beyond about 105° F. Also, the container is kept away from the engine and is cooled by air, to avoid heating the container. If the container should be heated so that gaseous ammonia begins to accumulate under pressure and the pressure exceeds a certain limit (e.g. 2 psi), a relief valve 60 (FIG. 1) will slowly vent the gaseous ammonia into the atmosphere. The rate of ammonia vented is very small, so it is not dangerous. A check valve 61 (FIG. 1) can admit air to avoid a vacuum above the liquid when the liquid is withdrawn.
  • The tube 36 that carries the ammonia-water mixture has a portion 62 that is wrapped about the exhaust conduit 16, to rapidly heat the ammonia-water mixture that passes through the tube 36 to the injection location 40.
  • FIG. 4 indicates how the ammonia may be separated from the water at a separation station 68, before injection of the ammonia into the exhaust conduit. Initially, the mixture 70 at a temperature such as 75° F. passes through the tube 36, to the tube portion 62 that is in a heat-exchange relationship with the exhaust conduit, so material within the tube portion 62 is rapidly heated. With the initial percent of ammonia being about 25%, the ammonia is not released as a gas until the mixture reaches the location 72 which is at about 105° F. Progressively more ammonia is released as the temperature of the mixture progressively increases. At the location 74, the mixture has a temperature of about 200° F., and only a few percent of ammonia remains in the mixture. The rest of the ammonia, indicated at 80, continues along a tube end portion 82, that carries the ammonia along a path 83 to an injector shown at 84 in FIG. 4. The injector can be of the type described in our earlier U.S. Pat. No. 5,992,141, which results in rapid heating of the gaseous ammonia prior to its injection into the very high temperature exhaust gasses, to activate the ammonia (break down some of the ammonia into its constituents) for injection into the exhaust gas stream.
  • The liquid 90 shown in FIG. 4 which moves along a path 91, contains only a very small percent of ammonia, and is disposed of. One way to dispose of it, indicated in FIG. 1, is to carry the liquid with a very small percent of ammonia along a tube 92 for injection at 94 into the exhaust pipe. The location 94 is a location where the temperature of the exhaust gasses have been reduced to perhaps 250° F., in which case the small quantity of injected water will evaporate and become part of the exhaust gas stream that is admitted into the atmosphere. It should be noted that small pumps may be located in the injection system 30 where pressure increases are required. In FIG. 1, the metering valve 34 is controlled by a circuit 100 that also controls a fuel injector 102 that injects fuel from a fuel line 104 into the engine cylinders. As discussed in my earlier U.S. Pat. No. 5,992,141, this varies the amount of ammonia in accordance with the load on the engine, to more effectively neutralize nitrogen oxides.
  • FIG. 6 illustrates a system 110 which includes a container 112 that contains the mixture 70 of ammonia (NH3) and water (HO2). Other ingredients can be added to the mixture 70, but applicant prefers that most of the mixture be water and ammonia. The ammonia is required to reduce nitrogen oxides and the water is useful to retain the ammonia and is a liquid that is easily disposed of because of its benign characteristics. In the system 110 of FIG. 6, applicant passes the mixture 70, which may have perhaps 25% ammonia by weight, and water, directly through a nozzle 84 that lies in the exhaust gas conduits 16, at an upstream location near or in the exhaust manifold. This system has the disadvantage that water is injected with the ammonia into the hot exhaust gasses, and tends to cool the exhaust gasses more rapidly. However, the amount of water and ammonia is very small, so the cooling effect of the water is very small. This system also has the disadvantage that the ammonia is heated only moderately by the hot nozzle prior to injection into the exhaust gas stream, so only a low percent of the ammonia is activated to break down the ammonia into its components (NH2 and NH) prior to injection. However, the simplicity of the system 110 can make it useful even if its effectiveness in reducing nitrogen oxides is not as great.
  • Thus, the invention provides a system for reducing nitrogen oxides in the exhaust gasses of an engine by the injection of ammonia into the exhaust gasses, which facilitates storage of the ammonia. The ammonia is stored as a mixture of ammonia and water (other liquids can be present), with the percent of ammonia preferably being between about 15% and 50% to avoid the generation of pressured ammonia gas. In one system, the mixture is heated to convert most of the ammonia into its gaseous state and separate it from the water that still remains liquid, and with the gaseous ammonia being further heated to activate at least a portion of it and then being injected into the hot exhaust gasses near or in the exhaust gas manifold. In a simpler system, the ammonia and water mixture 15 flowed towards the exhaust gas conduit and both ammonia and water are injected into the exhaust conduit.
  • Although particular embodiments of the invention have been described and illustrated herein, it is recognized that modifications and variations may readily occur to those skilled in the art, and consequently, it is intended that the claims be interpreted to cover such modifications and equivalents.

Claims (8)

1. In an engine which includes means for combusting hydrocarbons in air to produce work wherein said means also produces a stream of exhaust gasses that contain nitrogen oxides, with the engine having an exhaust conduit through which the exhaust gasses are passed before being emitted into the atmosphere, the improvement comprising:
a container;
a liquid mixture of ammonia and water in said container, said container being stored away from said means for combusting to minimize heating;
an injector apparatus coupled to said liquid in said container and to said exhaust conduit, said injector apparatus being constructed to inject at least ammonia of said mixture into said exhaust conduit.
2. The engine described in claim 1 wherein:
said mixture of ammonia and water in said container includes about 25% ammonia and about 75% water.
3. The engine described in claim 1 wherein:
said injector apparatus includes a tube that carries said liquid mixture, said tube lying in a heat-exchange relationship with said exhaust conduit to use the heat of the exhaust gasses to heat the liquid mixture of ammonia and water.
4. The engine described in claim 1 wherein:
said injector apparatus includes a tube that carries said mixture of ammonia and water from said source, and a nozzle coupled to said tube, said injector apparatus being constructed to inject said mixture of ammonia and water through said nozzle into said exhaust conduit.
5. In an engine which has an engine block with cylinders where hydrocarbons are combusted in air to produce work, and which has an exhaust conduit that carries away a stream of exhaust gasses that contain nitrogen oxides, a source of ammonia and an injection apparatus that is coupled to said source and that injects ammonia into the conduit to reduce nitrogen oxides, the improvement wherein:
said source of ammonia comprises a container and a liquid mixture of ammonia and water in said container, said container being thermally isolated from said engine block and said exhaust conduit.
said injection apparatus is constructed to inject ammonia and at least some of the water into said exhaust conduit.
6. The engine described in claim 5 wherein:
said injector apparatus includes a tube that carries said liquid mixture and that lies in a heat-exchange relationship with said exhaust conduit to use the heat of the exhaust gasses to heat the mixture of ammonia and water.
7. The engine described in claim 5 wherein:
said mixture of ammonia and water in said container includes about 25% ammonia and 75% water.
8. A method for reducing nitrogen oxide emission from an engine that has an engine block with cylinders where hydrocarbons are combusted in air to produce work, and which has an exhaust conduit that carries away a stream of exhaust gasses that contain nitrogen oxides, comprising:
storing a liquid mixture of ammonia and water in a container while thermally isolating the container from said engine block and said exhaust conduit;
passing said mixture from said container to an injector apparatus, and injecting ammonia and water into said exhaust conduit at a location downstream of said engine block.
US11/046,042 2002-04-24 2005-01-28 Ammonia storage and injection in NOx control Abandoned US20050129599A1 (en)

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070212287A1 (en) * 2003-11-05 2007-09-13 Urea Casale S.A. Method for the Treatment of Combustion Flue Gas
US20080066452A1 (en) * 2006-09-18 2008-03-20 Christopher Oberski Engine-Off Ammonia Vapor Management System and Method
US20080066453A1 (en) * 2006-09-18 2008-03-20 Christopher Oberski Management of a Plurality of Reductants for Selective Catalytic Reduction
US20080069750A1 (en) * 2006-09-18 2008-03-20 Christopher Oberski Ammonia Vapor Storage and Purge System and Method
US20080223021A1 (en) * 2007-03-15 2008-09-18 Furqan Shaikh Ammonia vapor management system and method
US8206470B1 (en) * 2005-08-03 2012-06-26 Jacobson William O Combustion emission-reducing method
WO2013162526A1 (en) * 2012-04-24 2013-10-31 International Engine Intellectual Property Company, Llc Biasing of ammonia lines to facilitate canister removal and insertion
US8677736B2 (en) 2010-03-05 2014-03-25 Toyota Jidosha Kabushiki Kaisha Exhaust gas purification apparatus of an internal combustion engine

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6852292B2 (en) * 2002-04-24 2005-02-08 Kleenair Systems, Inc. Ammonia storage and injection in NOx control
TR200803199T1 (en) * 2004-11-12 2008-12-22 The Babcock & Wilcox Company SNCR distribution grid.
JP4845012B2 (en) * 2006-03-31 2011-12-28 Udトラックス株式会社 Breather device for liquid tank and exhaust purification device for engine
WO2010039683A2 (en) * 2008-09-30 2010-04-08 Cummins Filtration Ip, Inc. Urea injector nozzle
JP5564989B2 (en) * 2010-02-26 2014-08-06 いすゞ自動車株式会社 Breather pipe structure of liquid reductant storage tank
JP5581790B2 (en) * 2010-04-22 2014-09-03 いすゞ自動車株式会社 Ammonia supply system to SCR equipment
JP5751165B2 (en) * 2011-12-28 2015-07-22 いすゞ自動車株式会社 Ammonia supply system to SCR converter
KR101527719B1 (en) * 2013-10-14 2015-06-11 한국기계연구원 An ammonia gas generator by using solid ammonium salt
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EP3333386B1 (en) 2016-12-12 2019-08-28 Perkins Engines Company Limited Injector deposit dissolution system and method
JP7063016B2 (en) * 2018-03-07 2022-05-09 いすゞ自動車株式会社 Post-processing equipment
US10920645B2 (en) 2018-08-02 2021-02-16 Ford Global Technologies, Llc Systems and methods for on-board monitoring of a passive NOx adsorption catalyst
FR3117161A1 (en) * 2020-12-04 2022-06-10 Faurecia Systemes D'echappement Exhaust gas post-treatment device

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3834359A (en) * 1971-04-30 1974-09-10 Safer Co Ltd Noxious gas minimizing method and apparatus for an internal-combustion engine
US4314345A (en) * 1978-01-23 1982-02-02 Mitsubishi Jukogyo Kabushiki Kaishi Controlling the injection of ammonia in a dry type exhaust gas denitration process
US4328020A (en) * 1980-11-24 1982-05-04 Ppg Industries, Inc. Melting glass with reduced NOx emissions
US5992141A (en) * 1996-04-02 1999-11-30 Kleen Air Systems, Inc. Ammonia injection in NOx control
US6093380A (en) * 1998-10-16 2000-07-25 Siirtec Nigi, S.P.A. Method and apparatus for pollution control in exhaust gas streams from fossil fuel burning facilities
US6146605A (en) * 1999-07-26 2000-11-14 Hera, Llc Combined SCR/SNCR process
US6852292B2 (en) * 2002-04-24 2005-02-08 Kleenair Systems, Inc. Ammonia storage and injection in NOx control

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3785359A (en) * 1970-03-28 1974-01-15 T Whittaker Windshield wash water heater
JPS5636971B2 (en) * 1974-05-08 1981-08-27
US4409931A (en) * 1976-02-13 1983-10-18 Owen, Wickersham & Erickson Combustion and pollution control system
US4274390A (en) * 1979-03-19 1981-06-23 Shinsuke Azuma Automotive hot water heater
DE3872536D1 (en) * 1987-02-11 1992-08-13 Babcock Anlagen Gmbh METHOD FOR MIXING AMMONIA IN A FLUE OF FLUE.
DE3910241C1 (en) * 1989-03-30 1990-10-04 Webasto Ag Fahrzeugtechnik, 8035 Stockdorf, De
US5224346A (en) * 1991-05-16 1993-07-06 James W. Davis Engine NOx reduction system
EP0585458B1 (en) * 1992-03-19 1997-11-05 The Nippon Signal Co. Ltd. Device for sensing aircraft
DE19713136A1 (en) * 1997-03-27 1998-10-01 Abb Patent Gmbh Non-catalytic process and assembly converts oxides ofnitrogen and ammonia
US6048510A (en) * 1997-09-30 2000-04-11 Coal Tech Corporation Method for reducing nitrogen oxides in combustion effluents
EP1085939B1 (en) * 1998-05-11 2003-08-06 Siemens Aktiengesellschaft Method and device for selective catalytic reduction of nitrogen oxides in a gaseous medium containing oxygen

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3834359A (en) * 1971-04-30 1974-09-10 Safer Co Ltd Noxious gas minimizing method and apparatus for an internal-combustion engine
US4314345A (en) * 1978-01-23 1982-02-02 Mitsubishi Jukogyo Kabushiki Kaishi Controlling the injection of ammonia in a dry type exhaust gas denitration process
US4328020A (en) * 1980-11-24 1982-05-04 Ppg Industries, Inc. Melting glass with reduced NOx emissions
US5992141A (en) * 1996-04-02 1999-11-30 Kleen Air Systems, Inc. Ammonia injection in NOx control
US6093380A (en) * 1998-10-16 2000-07-25 Siirtec Nigi, S.P.A. Method and apparatus for pollution control in exhaust gas streams from fossil fuel burning facilities
US6146605A (en) * 1999-07-26 2000-11-14 Hera, Llc Combined SCR/SNCR process
US6852292B2 (en) * 2002-04-24 2005-02-08 Kleenair Systems, Inc. Ammonia storage and injection in NOx control

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070212287A1 (en) * 2003-11-05 2007-09-13 Urea Casale S.A. Method for the Treatment of Combustion Flue Gas
US7566431B2 (en) * 2003-11-05 2009-07-28 Urea Casale S.A. Method for the treatment of combustion flue gas
US8206470B1 (en) * 2005-08-03 2012-06-26 Jacobson William O Combustion emission-reducing method
US7726118B2 (en) 2006-09-18 2010-06-01 Ford Global Technologies, Llc Engine-off ammonia vapor management system and method
US20080069750A1 (en) * 2006-09-18 2008-03-20 Christopher Oberski Ammonia Vapor Storage and Purge System and Method
US20080066453A1 (en) * 2006-09-18 2008-03-20 Christopher Oberski Management of a Plurality of Reductants for Selective Catalytic Reduction
US8132404B2 (en) 2006-09-18 2012-03-13 Ford Global Technologies, Llc Ammonia vapor storage and purge system and method
US7770384B2 (en) 2006-09-18 2010-08-10 Ford Global Technologies, Llc Ammonia vapor storage and purge system and method
US20100236219A1 (en) * 2006-09-18 2010-09-23 Ford Global Technologies, Llc Engine-off ammonia vapor management system and method
US20100319317A1 (en) * 2006-09-18 2010-12-23 Ford Global Technologies, Llc Ammonia vapor storage and purge system and method
US8209961B2 (en) 2006-09-18 2012-07-03 Ford Global Technologies, Llc Engine-off ammonia vapor management system and method
US8015801B2 (en) 2006-09-18 2011-09-13 Ford Global Technologies, Llc Management of a plurality of reductants for selective catalytic reduction
US20080066452A1 (en) * 2006-09-18 2008-03-20 Christopher Oberski Engine-Off Ammonia Vapor Management System and Method
US20080223021A1 (en) * 2007-03-15 2008-09-18 Furqan Shaikh Ammonia vapor management system and method
US20110232611A1 (en) * 2007-03-15 2011-09-29 Ford Global Technologies, Llc Ammonia vapor management system and method
US7954311B2 (en) 2007-03-15 2011-06-07 Ford Global Technologies, Llc Ammonia vapor management system and method
US8621848B2 (en) 2007-03-15 2014-01-07 Ford Global Technologies, Llc Ammonia vapor management system and method
US8677736B2 (en) 2010-03-05 2014-03-25 Toyota Jidosha Kabushiki Kaisha Exhaust gas purification apparatus of an internal combustion engine
WO2013162526A1 (en) * 2012-04-24 2013-10-31 International Engine Intellectual Property Company, Llc Biasing of ammonia lines to facilitate canister removal and insertion

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ATE382418T1 (en) 2008-01-15
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WO2003091155A1 (en) 2003-11-06
JP2005524012A (en) 2005-08-11

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