US3839535A - Internal combustion engine exhaust treatment - Google Patents
- ️Tue Oct 01 1974
US3839535A - Internal combustion engine exhaust treatment - Google Patents
Internal combustion engine exhaust treatment Download PDFInfo
-
Publication number
- US3839535A US3839535A US00296650A US29665072A US3839535A US 3839535 A US3839535 A US 3839535A US 00296650 A US00296650 A US 00296650A US 29665072 A US29665072 A US 29665072A US 3839535 A US3839535 A US 3839535A Authority
- US
- United States Prior art keywords
- exhaust gas
- flow
- combustion engine
- internal combustion
- fins Prior art date
- 1971-02-10 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.)
- Expired - Lifetime
Links
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 10
- 239000007789 gas Substances 0.000 claims abstract description 34
- 239000003054 catalyst Substances 0.000 claims abstract description 13
- 229910052751 metal Inorganic materials 0.000 claims abstract description 12
- 239000002184 metal Substances 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims abstract description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 7
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 7
- 239000001301 oxygen Substances 0.000 claims abstract description 7
- 230000009467 reduction Effects 0.000 claims abstract description 4
- 230000003197 catalytic effect Effects 0.000 description 12
- 238000004804 winding Methods 0.000 description 9
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 7
- 229910052802 copper Inorganic materials 0.000 description 7
- 239000010949 copper Substances 0.000 description 7
- 238000001816 cooling Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 230000008901 benefit Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241000005139 Lycium andersonii Species 0.000 description 1
- 238000002679 ablation Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 150000002611 lead compounds Chemical class 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000005201 scrubbing Methods 0.000 description 1
- 125000006850 spacer group Chemical group 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/0205—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust using heat exchangers
-
- 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
-
- 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
- B01D53/46—Removing components of defined structure
- B01D53/62—Carbon oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/72—Copper
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N13/00—Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00
- F01N13/009—Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00 having two or more separate purifying devices arranged in series
- F01N13/0097—Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00 having two or more separate purifying devices arranged in series the purifying devices are arranged in a single housing
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/04—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust using liquids
- F01N3/043—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust using liquids without contact between liquid and exhaust gases
- F01N3/046—Exhaust manifolds with cooling jacket
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust 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
- F01N3/18—Exhaust 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
- F01N3/20—Exhaust 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust 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
- F01N3/24—Exhaust 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 constructional aspects of converting apparatus
- F01N3/28—Construction of catalytic reactors
- F01N3/2803—Construction of catalytic reactors characterised by structure, by material or by manufacturing of catalyst support
- F01N3/2807—Metal other than sintered metal
- F01N3/281—Metallic honeycomb monoliths made of stacked or rolled sheets, foils or plates
- F01N3/2821—Metallic honeycomb monoliths made of stacked or rolled sheets, foils or plates the support being provided with means to enhance the mixing process inside the converter, e.g. sheets, plates or foils with protrusions or projections to create turbulence
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N9/00—Electrical control of exhaust gas treating apparatus
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N13/00—Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00
- F01N13/14—Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00 having thermal insulation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2240/00—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
- F01N2240/02—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being a heat exchanger
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2410/00—By-passing, at least partially, exhaust from inlet to outlet of apparatus, to atmosphere or to other device
-
- 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
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
-
- 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
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/40—Engine management systems
Definitions
- a catalytic reactor to be connected in series with ducting for hot gases containing CO comprises:
- This invention relates generally to pollution reduction, and more particularly concerns improvements in internal combustion engine exhaust treatment in catalytic reactors.
- the fin metal may advantageously consist of copper strip, corrugated and wound in a spiral about an axis extending longitudinally in the case, so that the corrugations and passages extend longitudinally therein.
- a pack may be easily formed and introduced into the case to maximize catalytic effectiveness by virtue of 3,839,535 Patented Oct. 1, 1974 great surface area while minimizing back pressure creation.
- corrugations which may be formed to have saw-tooth configuration, with multiple spirally wound strips stacked endwise in the case.
- the latter may consist of aluminum or aluminum alloy, and there may be cooling means to assure that the exhaust gas temperature is such as to promote desired catalytic action.
- FIG. 1 is an elevation showing a reactor connected with an engine exhaust
- FIG. 2 is an enlarged section taken on line 2-2 of FIG. 1;
- FIG. 3 is a fragmentary section showing a modification
- FIG. 4 is a fragmentary section showing another modification
- FIG. 5 is a perspective showing of a portion of the catalytic reactor strip
- FIG. 6 is a section taken on line 6--6 of FIG. 5, and
- FIGS. 7 and 8 are fragmentary elevations showing still other modifications.
- an internal combustion engine 10 of Otto, Diesel or other cycle, has an exhaust manifold 11 connected with a tail pipe 12.
- a catalytic reactor 13 comprising a longitudinally elongated generally tubular case 14 having lengthwise spaced entrance and exit ports 15 and 16.
- the fins Contained within the tubular case are multiple metallic fins extended longitudinally in closely packed relation to form multiple flow passages for the engine exhaust, the passages being spaced apart transversely of the case interior.
- the fins may be defined as corrugations 17 on multiple metallic strips 18 each wound in a spiral about an axis 19 extending longitudinally in the case.
- the strips are stacked end to end in multiple sections, as shown.
- the striking of the tabs from the strip forms openings 21 communicating between the longitudinal passages 22 between such windings, so that hot exhaust gases may not only flow lengthwise in intimate contact with the windings, but may also be deflected by the tabs and through the openings to impinge against the strip winding surfaces. In this way, maximum contacting and scrubbing of the dispersed gases against the thin windings is achieved, for catalytic reaction.
- the corrugations may have saw tooth configuration in FIG. 2 cross section as defined by flat portions 18a and folds 18b; further the thickness of the Strip may with unusual advantage be between .004 and .007 inch; the crest to crest dimensions of the saw tooth corrugations may lie between A and inch; the gap between adjacent windings may be about to inch; and the crest to trough dimensions of the saw tooth corrugations may lie between A and /2 inch.
- the fin or strip metal consists of a catalyst which, when contacted by the hot exhaust gases, reduces the oxide content of the latter thereby to increase the oxygen content in the exhaust discharge from the exit port 16.
- the fin metal consists essentially of copper, as for example pure copper which when contacted by the hot exhaust gases produces the following reactions with respect to CO CO, N and NO, and at the indicated temperatures:
- An important aspect of the invention concerns the con-*, trol or maintenance of exhaust gas temperature at a level, or levels such as promote desired catalytic action, as described.
- Such control may be efiected by exhaust gas cooling in the line 12, as for example the line 12c which may be unrestricted or may include a valve 42 as shown (which may be open for unrestricted flow).
- the exhaust may be pre-cooled in a heat exchanger 43 in line 12b, as indicated and for this purpose valve 44 in that line may be opened to desired degree.
- the intent is to provide such control (manual or automatic) as will ensure maintenance of the temperature of the exhaust gas entering the reactor 13 within a range such as will promote the desired catalytic action for the copper fin reactor as described. That range is between about 150 F.
- An exhaust temperature sensor may be provided at 45 at the entrance to the reactor, to provide input for the control and actuator 46 for one or both valves 42 and 44.
- particulate matter such as lead compounds, carbon residues and dirt will be passed through a reactor constructed in accordance with trapped in the catalytic bed structure.
- fuel does not contaminate copper.
- Equation (7) above shows the manner in which water is produced from the engine exhaust hydrocarbons; also, water is condensed out of the exhaust gases flowing through the reactor. Such produced and condensed water may be drained from the reactor, as for example via a drainage outlet in the case, shown at 40 in FIG. 1. Another method would be to collect the water in a gravity trap which may be periodically drained.
- the temperature of the strip material 18 should preferably be kept under 550 F., and for that purpose cooling of the case 14 may be enhanced as by the means shown for example in FIGS. 3 and 4.
- cooling fins 25 project from the case 26 which, together with the fins, may consist of aluminum or alloys thereof.
- a waterjacket 27 surrounds the case 28 to retain cooling water 29 therebetween.
- FIG. 1 also illustrates diffuser cones 30 and 31 at the entrance and exit ends of the reactor, to assure desired distribution of the exhaust flow through the many passages formed between the strip windings, and to prevent direct initial impingement of the exhaust gases on the catalyst, since such direct impingement of hot gases tends to erode and ablate the thin catalyst sections.
- a perforated diffuser plate 32 extends across the interior of the shell 33 containing the strip windings or fill 34, at
- the reactor may be used, as in a submarine or space station to process air breathed by the crew to convert CO to C and 0 with attendant advantages such as extending the underwater cruise time of the submarine, or replenishing the oxygen content of the space station atmosphere.
- the device may, in fact, be used advantageously anywhere to decrease the C0, C0 and NO content of the atmosphere.
- the method of treating internal combustion engine exhaust gas flow to reduce their oxide content and to increase oxygen content of the gases that includes:
- the method of claim 1 including the step of confining the gas flow within a flow zone wherein the fins are located to extend generally lengthwise of the flow.
- controlling step includes pre-cooling the exhaust gas prior to contact thereof with said fins.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Combustion & Propulsion (AREA)
- Health & Medical Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- Biomedical Technology (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Toxicology (AREA)
- Exhaust Gas After Treatment (AREA)
- Catalysts (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
1. THE METHOD OF TREATING INTERNAL COMBUSTION ENGINE EXHAUST GAS FLOW OF REDUCED THEIR OXIDE CONTENT AND TO INCREASE OXYGEN CONTENT OF THE GASES THAT INCLUDES: (A) INITIALLY CONTROLLING THE EXHAUST GAS TEMPERATURE TO LIE WITHIN A RANGE OF FROM ABOUT 150*F. AND 650*F., ABD (B) THEREAFTER EFFECTONG INTIMATE CONTACT OF THE CONTROLLED TEMPERATURE GASEOUS FLOW WITH EXPOSED CATALYST METAL IN THE FORM OF MULTIPLE FINS WHILE DIRECTING SAID FLOW GENERALLY PARALLEL TO SAID FINS, THE CATALYST METAL CONSISTING ESSENTIALLY OF COPPER, THEREBY TO CATALYSE THE REDUCTION OF THE OXIDE CONTENT OF THE EXHAUST GAS.
Description
COMBUSTION ENGINE EXHAUST TREATMENT Original Filed Feb. 10, 1971 D. P. ASHBURN INTERNAL United States Patent 3,839,535 INTERNAL COMBUSTION ENGINE EXHAUST TREATMENT Dillion P. Ashburn, Ogden, Utah, assignor to New Products Corporation, Ogden, Utah Original application Feb. 10, 1971, Ser. No. 114,175, now Patent No. 3,716,344. Divided and this application Oct. 11, 1972, Ser. No. 296,650
Int. Cl. B01d 47/00 US. Cl. 423-213.2 Claims ABSTRACT OF THE DISCLOSURE A catalytic reactor to be connected in series with ducting for hot gases containing CO comprises:
(a) a longitudinally elongated generally tubular case having lengthwise spaced entrance and exit ports, the entrance port to receive said gas at elevated temperature, and
(b) multiple metallic fins extending generally longitudinally in the case and in closely packed relation to form multiple flow passages for said gas, the passages being spaced apart transversely of the case,
(c) and the fin surface metal consisting of a copper catalyst which when contacted by the hot gas reduces the CO content thereby to increase the oxygen content in the gas discharge from said exit port.
This is a division of application Ser. No. 114,175, filed Feb. 10, 1971 now US. Pat. 3,716,344.
BACKGROUND OF THE INVENTION This invention relates generally to pollution reduction, and more particularly concerns improvements in internal combustion engine exhaust treatment in catalytic reactors.
In the past, catalytic reactors have suffered from deficiencies such as excessive complexity, the creation of unacceptable back pressure, and failure to remove pollutants to the extent sought or desired in accordance with present day standards. None of such prior reactors have to my knowledge embodied those combinations of unusually advantageous features of construction, mode of operation and desirable results characterized by the present invention.
SUMMARY OF THE INVENTION It is a major object of the invention to provide a catalytic reactor connectible in series with internal combustion engine exhaust ducting and comprising a longitudinally elongated generally tubular case having lengthwise spaced entrance an exit ports; and multiple metallic fins extending generally longitudinally in the case and in closely packed relation to form multiple flow passages for entering exhaust, the passages being spaced apart transversely of the case; and the fin metal consisting of a catalyst which when contacted by the hot exhaust gases reduces their oxide content so as to increase the oxygen content in the exhaust discharge from the exit port. As will be seen, the fin metal may advantageously consist of copper strip, corrugated and wound in a spiral about an axis extending longitudinally in the case, so that the corrugations and passages extend longitudinally therein. Further, there may be tabs on the strip struck out to project and maintain successive windings spaced apart, and also to form openings through the strip to promote lateral movement of exhaust gases and their intimate contact with the strip metal to promote the reaction. In this way, a pack may be easily formed and introduced into the case to maximize catalytic effectiveness by virtue of 3,839,535 Patented Oct. 1, 1974 great surface area while minimizing back pressure creation.
Additional objects include the corrugations which may be formed to have saw-tooth configuration, with multiple spirally wound strips stacked endwise in the case. The latter may consist of aluminum or aluminum alloy, and there may be cooling means to assure that the exhaust gas temperature is such as to promote desired catalytic action.
These and other objects and advantages of the invention, as well as the details of illustrative embodiment, will be more fully understood from the following descriptio and drawings, in which:
DRAWING DESCRIPTION FIG. 1 is an elevation showing a reactor connected with an engine exhaust;
FIG. 2 is an enlarged section taken on line 2-2 of FIG. 1;
FIG. 3 is a fragmentary section showing a modification;
FIG. 4 is a fragmentary section showing another modification;
FIG. 5 is a perspective showing of a portion of the catalytic reactor strip;
FIG. 6 is a section taken on
line6--6 of FIG. 5, and
FIGS. 7 and 8 are fragmentary elevations showing still other modifications.
DETAILED DESCRIPTION In FIG. 1, an
internal combustion engine10, of Otto, Diesel or other cycle, has an exhaust manifold 11 connected with a
tail pipe12. Connected in series with the latter is a
catalytic reactor13 comprising a longitudinally elongated generally
tubular case14 having lengthwise spaced entrance and
exit ports15 and 16.
Contained within the tubular case are multiple metallic fins extended longitudinally in closely packed relation to form multiple flow passages for the engine exhaust, the passages being spaced apart transversely of the case interior. For example, the fins may be defined as corrugations 17 on multiple
metallic strips18 each wound in a spiral about an axis 19 extending longitudinally in the case. The strips are stacked end to end in multiple sections, as shown. Typically, there are
tabs20 on and struck out from each strip to projects therefrom and act as spacers for maintaining the spiral windings closely spaced apart. 'Further, the striking of the tabs from the strip forms
openings21 communicating between the longitudinal passages 22 between such windings, so that hot exhaust gases may not only flow lengthwise in intimate contact with the windings, but may also be deflected by the tabs and through the openings to impinge against the strip winding surfaces. In this way, maximum contacting and scrubbing of the dispersed gases against the thin windings is achieved, for catalytic reaction.
Note that the corrugations may have saw tooth configuration in FIG. 2 cross section as defined by
flat portions18a and folds 18b; further the thickness of the Strip may with unusual advantage be between .004 and .007 inch; the crest to crest dimensions of the saw tooth corrugations may lie between A and inch; the gap between adjacent windings may be about to inch; and the crest to trough dimensions of the saw tooth corrugations may lie between A and /2 inch.
The fin or strip metal consists of a catalyst which, when contacted by the hot exhaust gases, reduces the oxide content of the latter thereby to increase the oxygen content in the exhaust discharge from the
exit port16. Typically, the fin metal consists essentially of copper, as for example pure copper which when contacted by the hot exhaust gases produces the following reactions with respect to CO CO, N and NO, and at the indicated temperatures:
In the above, it will be noted that 0 N and C are produced, and that in reaction (6) the CuO content is preserved.
In a test performed upon an internal combustion engine exhaust, the engine running at 1,500 r.p.m. the following exhaust constituent values as measured on a gas chromatograph were observed before and after the exhaust was the
entrance end35, to assure desired exhaust flow distribution and to prevent such initial direct impingement of hot exhaust on the thin catalyst fins. Flow ditfuser and strainer devices are shown at 50 and 51 in FIG. .8, and consist of holes in bafiles 52-54.
An important aspect of the invention concerns the con-*, trol or maintenance of exhaust gas temperature at a level, or levels such as promote desired catalytic action, as described. Such control may be efiected by exhaust gas cooling in the
line12, as for example the line 12c which may be unrestricted or may include a
valve42 as shown (which may be open for unrestricted flow). Alternatively, the exhaust may be pre-cooled in a heat exchanger 43 in
line12b, as indicated and for this
purpose valve44 in that line may be opened to desired degree. The intent is to provide such control (manual or automatic) as will ensure maintenance of the temperature of the exhaust gas entering the
reactor13 within a range such as will promote the desired catalytic action for the copper fin reactor as described. That range is between about 150 F. and 650 F. Below that range, proper catalytic action will not occur, and above that range, excessive CO will be produced and the life of the catalyst is substantially decreased by chemical action and structural ablation. An exhaust temperature sensor may be provided at 45 at the entrance to the reactor, to provide input for the control and
actuator46 for one or both
valves42 and 44.
It should also be mentioned that particulate matter such as lead compounds, carbon residues and dirt will be passed through a reactor constructed in accordance with trapped in the catalytic bed structure. In this regard, leaded the invention: fuel does not contaminate copper.
A Scale Percent Read A Scale Percent 69.4. 52. 9 10.
5s12. 95 1o. 4 10. 4 2. 0s 2. 15 9. 3 1.86 2. s9 78. 4 68. 0 13. 60 17. 66. 0 66. 00 80. 90 62. 0 62. 0 62. 00 79. 00 31.2 3.12 3.84 7.0 7.0 .70 .891
Total 81.56 100.58 78.38 99.441
In the above, note that the 0 content was substantially increased, whereas the CO content was substantially reduced. The 0 percentage content at the discharge of the reactor is just below the normal 0 content for air which is 220.99%.
It should also be observed that due to the essentially straight-through construction of the reactor, the back pressure created is very low. Further, it has been found to be similarly workable with both unleaded and leaded gasoline used as fuel for the engine.
Equation (7) above shows the manner in which water is produced from the engine exhaust hydrocarbons; also, water is condensed out of the exhaust gases flowing through the reactor. Such produced and condensed water may be drained from the reactor, as for example via a drainage outlet in the case, shown at 40 in FIG. 1. Another method would be to collect the water in a gravity trap which may be periodically drained.
The temperature of the
strip material18 should preferably be kept under 550 F., and for that purpose cooling of the
case14 may be enhanced as by the means shown for example in FIGS. 3 and 4. In FIG. 3, cooling
fins25 project from the
case26 which, together with the fins, may consist of aluminum or alloys thereof. In FIG. 4 a
waterjacket27 surrounds the
case28 to retain cooling
water29 therebetween.
FIG. 1 also illustrates
diffuser cones30 and 31 at the entrance and exit ends of the reactor, to assure desired distribution of the exhaust flow through the many passages formed between the strip windings, and to prevent direct initial impingement of the exhaust gases on the catalyst, since such direct impingement of hot gases tends to erode and ablate the thin catalyst sections. In FIG. 7 a
perforated diffuser plate32 extends across the interior of the
shell33 containing the strip windings or fill 34, at
Further, the reactor may be used, as in a submarine or space station to process air breathed by the crew to convert CO to C and 0 with attendant advantages such as extending the underwater cruise time of the submarine, or replenishing the oxygen content of the space station atmosphere. The device may, in fact, be used advantageously anywhere to decrease the C0, C0 and NO content of the atmosphere.
I claim:
1. The method of treating internal combustion engine exhaust gas flow to reduce their oxide content and to increase oxygen content of the gases that includes:
(a) initially controlling the exhaust gas temperature to lie within a range of from about F. and 650 F., and
(b) thereafter effecting intimate contact of the controlled temperature gaseous flow with exposed catalyst metal in the form of multiple fins while directing said flow generally parallel to said fins, the catalyst metal consisting essentially of copper, thereby to catalyse the reduction of the oxide content of the exhaust gas.
2. The method of claim 1 including the step of confining the gas flow within a flow zone wherein the fins are located to extend generally lengthwise of the flow.
3. The method of claim 2 wherein said controlling step includes pre-cooling the exhaust gas prior to contact thereof with said fins.
4. The method of claim 3 including sensing the exhaust gas Emperature proximate said zone.
5. The method of claim 2 including the step of draining water condensate from said zone.
(References on following page) References Cited UNITED STATES PATENTS Pomykala 423-212 Miley 55-Dig. 30 5 Bettega 60-298 Pahnke et a1. 23288 X Houdry 423-247 X FOREIGN PATENTS 2/ 1930 Great Britain.
GEORGE O. PETERS, Primary Examiner US. Cl. X.R.
Claims (1)
1. THE METHOD OF TREATING INTERNAL COMBUSTION ENGINE EXHAUST GAS FLOW OF REDUCED THEIR OXIDE CONTENT AND TO INCREASE OXYGEN CONTENT OF THE GASES THAT INCLUDES: (A) INITIALLY CONTROLLING THE EXHAUST GAS TEMPERATURE TO LIE WITHIN A RANGE OF FROM ABOUT 150*F. AND 650*F., ABD (B) THEREAFTER EFFECTONG INTIMATE CONTACT OF THE CONTROLLED TEMPERATURE GASEOUS FLOW WITH EXPOSED CATALYST METAL IN THE FORM OF MULTIPLE FINS WHILE DIRECTING SAID FLOW GENERALLY PARALLEL TO SAID FINS, THE CATALYST METAL CONSISTING ESSENTIALLY OF COPPER, THEREBY TO CATALYSE THE REDUCTION OF THE OXIDE CONTENT OF THE EXHAUST GAS.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US00296650A US3839535A (en) | 1971-02-10 | 1972-10-11 | Internal combustion engine exhaust treatment |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11417571A | 1971-02-10 | 1971-02-10 | |
US00296650A US3839535A (en) | 1971-02-10 | 1972-10-11 | Internal combustion engine exhaust treatment |
Publications (1)
Publication Number | Publication Date |
---|---|
US3839535A true US3839535A (en) | 1974-10-01 |
Family
ID=26811882
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US00296650A Expired - Lifetime US3839535A (en) | 1971-02-10 | 1972-10-11 | Internal combustion engine exhaust treatment |
Country Status (1)
Country | Link |
---|---|
US (1) | US3839535A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4104360A (en) * | 1973-02-05 | 1978-08-01 | Standard Oil Company | Process for reducing oxides nitrogen in the exhaust gas from internal combustion engines |
EP0229352A1 (en) * | 1986-01-15 | 1987-07-22 | Siemens Aktiengesellschaft | Metallic catalyst body with protection from radiant heat |
WO1991001178A1 (en) * | 1989-07-18 | 1991-02-07 | Emitec Gesellschaft Für Emissionstechnologie Mbh | Honeycomb body with internal flow-conducting surfaces, in particular catalyst body for motor vehicles |
WO1994026411A1 (en) * | 1993-05-13 | 1994-11-24 | Siemens Aktiengesellschaft | Plate-type catalytic converter |
US5403559A (en) * | 1989-07-18 | 1995-04-04 | Emitec Gesellschaft Fuer Emissionstechnologie | Device for cleaning exhaust gases of motor vehicles |
US5820832A (en) * | 1993-05-13 | 1998-10-13 | Siemens Aktiengesellschaft | Plate-type catalytic converter |
US6116022A (en) * | 1996-07-03 | 2000-09-12 | Outboard Marine Corporation | Catalytic reactor for marine application |
EP2088295A2 (en) | 2008-02-11 | 2009-08-12 | Pierburg GmbH | Method for controlling a motor vehicle combustion engine assembly |
-
1972
- 1972-10-11 US US00296650A patent/US3839535A/en not_active Expired - Lifetime
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4104360A (en) * | 1973-02-05 | 1978-08-01 | Standard Oil Company | Process for reducing oxides nitrogen in the exhaust gas from internal combustion engines |
EP0229352A1 (en) * | 1986-01-15 | 1987-07-22 | Siemens Aktiengesellschaft | Metallic catalyst body with protection from radiant heat |
WO1991001178A1 (en) * | 1989-07-18 | 1991-02-07 | Emitec Gesellschaft Für Emissionstechnologie Mbh | Honeycomb body with internal flow-conducting surfaces, in particular catalyst body for motor vehicles |
US5403559A (en) * | 1989-07-18 | 1995-04-04 | Emitec Gesellschaft Fuer Emissionstechnologie | Device for cleaning exhaust gases of motor vehicles |
WO1994026411A1 (en) * | 1993-05-13 | 1994-11-24 | Siemens Aktiengesellschaft | Plate-type catalytic converter |
US5820832A (en) * | 1993-05-13 | 1998-10-13 | Siemens Aktiengesellschaft | Plate-type catalytic converter |
US6116022A (en) * | 1996-07-03 | 2000-09-12 | Outboard Marine Corporation | Catalytic reactor for marine application |
EP2088295A2 (en) | 2008-02-11 | 2009-08-12 | Pierburg GmbH | Method for controlling a motor vehicle combustion engine assembly |
EP2088295A3 (en) * | 2008-02-11 | 2010-04-07 | Pierburg GmbH | Method for controlling a motor vehicle combustion engine assembly |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3716344A (en) | 1973-02-13 | Internal combustion engine exhaust catalytic reactor |
US3295919A (en) | 1967-01-03 | Method of treating exhaust gases of internal combustion engines |
US2071119A (en) | 1937-02-16 | Process and apparatus for treating furnace gases and exhaust gases from internal combustion engines |
US3067002A (en) | 1962-12-04 | Method of treating exhaust gases of internal combustion engines |
US1867325A (en) | 1932-07-12 | Process of removing carbon monoxide from exhaust gases |
US4519820A (en) | 1985-05-28 | Fitter apparatus for purifying exhaust gases |
US1522111A (en) | 1925-01-06 | Muffler for internal-combustion engines |
US5829250A (en) | 1998-11-03 | Series combination catalytic converter |
EP0234817B1 (en) | 1994-05-18 | Method and apparatus for denitration |
US3025132A (en) | 1962-03-13 | Method of oxidizing hydrocarbon constituents of exhaust gases |
US3839535A (en) | 1974-10-01 | Internal combustion engine exhaust treatment |
US4672809A (en) | 1987-06-16 | Catalytic converter for a diesel engine |
US2853367A (en) | 1958-09-23 | Cartridge type catalytic exhaust cleaner |
US3521429A (en) | 1970-07-21 | Muffler |
GB1328454A (en) | 1973-08-30 | Catalytic exhaust gas convertors |
CA2063684A1 (en) | 1992-09-22 | Exhaust gas filter and/or a catalytic converter |
US3853484A (en) | 1974-12-10 | Compact muffler scrubber |
US3718733A (en) | 1973-02-27 | Catalytic treatment of exhaust gases |
US3485593A (en) | 1969-12-23 | Exhaust treating device |
US3755120A (en) | 1973-08-28 | Internal combustion engine exhaust catalytic reactor, with electrical charge means |
JPH05285343A (en) | 1993-11-02 | Denitrification device |
US4701312A (en) | 1987-10-20 | Fluidized bed catalytic converter |
US3511617A (en) | 1970-05-12 | Catalytic muffler |
CA1101638A (en) | 1981-05-26 | Process |
US2828189A (en) | 1958-03-25 | Device for catalytically purifying exhaust gases |