CN102337986A - Tail gas ultra-high-pressure homogeneous deflagration zero-discharge assisting energy-saving machine main piece device - Google Patents
Tail gas ultra-high-pressure homogeneous deflagration zero-discharge assisting energy-saving machine main piece device Download PDFInfo
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- CN102337986A CN102337986A CN2010102305650A CN201010230565A CN102337986A CN 102337986 A CN102337986 A CN 102337986A CN 2010102305650 A CN2010102305650 A CN 2010102305650A CN 201010230565 A CN201010230565 A CN 201010230565A CN 102337986 A CN102337986 A CN 102337986A
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- 238000004200 deflagration Methods 0.000 title abstract 4
- 239000007789 gas Substances 0.000 claims abstract description 372
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 315
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 284
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 274
- 238000002485 combustion reaction Methods 0.000 claims abstract description 201
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 116
- 239000001257 hydrogen Substances 0.000 claims abstract description 116
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 116
- 230000002269 spontaneous effect Effects 0.000 claims abstract description 87
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 76
- 238000010438 heat treatment Methods 0.000 claims abstract description 56
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 38
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 38
- 239000000446 fuel Substances 0.000 claims abstract description 31
- 238000005474 detonation Methods 0.000 claims description 135
- 238000001833 catalytic reforming Methods 0.000 claims description 55
- 241000282326 Felis catus Species 0.000 claims description 29
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 24
- 239000001301 oxygen Substances 0.000 claims description 24
- 229910052760 oxygen Inorganic materials 0.000 claims description 24
- 238000004134 energy conservation Methods 0.000 claims description 15
- 238000000265 homogenisation Methods 0.000 claims description 14
- 230000008450 motivation Effects 0.000 claims description 12
- 239000003054 catalyst Substances 0.000 claims description 11
- 239000007921 spray Substances 0.000 claims description 11
- 238000004140 cleaning Methods 0.000 claims description 10
- 238000010304 firing Methods 0.000 claims description 7
- 238000000746 purification Methods 0.000 abstract description 15
- 238000000034 method Methods 0.000 abstract description 11
- 231100000086 high toxicity Toxicity 0.000 abstract description 9
- 230000006835 compression Effects 0.000 abstract description 8
- 238000007906 compression Methods 0.000 abstract description 8
- 230000003197 catalytic effect Effects 0.000 abstract description 5
- 239000010815 organic waste Substances 0.000 abstract description 5
- 239000007788 liquid Substances 0.000 abstract description 4
- 238000013329 compounding Methods 0.000 abstract 1
- 239000010808 liquid waste Substances 0.000 description 12
- 238000002347 injection Methods 0.000 description 9
- 239000007924 injection Substances 0.000 description 9
- 231100000331 toxic Toxicity 0.000 description 4
- 230000002588 toxic effect Effects 0.000 description 4
- 239000002918 waste heat Substances 0.000 description 4
- 238000006555 catalytic reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000000295 fuel oil Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 241001131796 Botaurus stellaris Species 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 230000002153 concerted effect Effects 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 230000006870 function Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000002407 reforming Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- QBUKAFSEUHGMMX-MTJSOVHGSA-N (5z)-5-[[3-(1-hydroxyethyl)thiophen-2-yl]methylidene]-10-methoxy-2,2,4-trimethyl-1h-chromeno[3,4-f]quinolin-9-ol Chemical compound C1=CC=2NC(C)(C)C=C(C)C=2C2=C1C=1C(OC)=C(O)C=CC=1O\C2=C/C=1SC=CC=1C(C)O QBUKAFSEUHGMMX-MTJSOVHGSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000002844 continuous effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 230000001131 transforming effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
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- 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
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- Output Control And Ontrol Of Special Type Engine (AREA)
Abstract
The invention discloses a tail gas ultra-high-pressure homogeneous deflagration zero-discharge assisting energy-saving machine main piece device, which adopts three systems: a system for preparing fuel steam through heating high-pollution high-toxicity high-concentration high-energy-content organic waste liquid water alcohol agents in tail gas afterheat utilization, a system for tail gas carbon dioxide multi-effect compounding catalytic purification and ultra-high-temperature ultra-high-speed ultra-high-pressure homogeneous compression ignition spontaneous combustion and deflagration burning purification, and a system for preparing high-pressure alcohol hydrogen mixed gas high-energy fuel from high-pollution high-toxicity high-concentration high-energy-content organic waste liquid water alcohol steam in afterheat utilization to improve the energy-saving device combustion support assistance of the engine power. The energy saving device of the complete combustion device adopting a high-temperature homogeneous compression ignition spontaneous combustion and deflagration complete burning purification method for ensuring the goal of standard reaching exhaust of the tail gas and adopting the afterheat utilization for preparing the nonbiodegradable high-pollution high-toxicity high-concentration high-energy-content organic waste liquid water alcohol steam into high-pressure alcohol hydrogen mixed gas high-energy fuel for realizing the consumption support assistance on the engine is a purifier device with the multi-effect purification function and is suitable for being used on an internal-combustion engine.
Description
Affiliated technical field
UTILIZATION OF VESIDUAL HEAT IN purified treatment, exhaust gases of internal combustion engines of organic liquid waste of highly toxic highly enriched Gao Hanneng that the present invention relates to a kind of high pollution of bio-refractory is heated to be the agent of water alcohol and tail gas is strengthened behind the fuel fume to burn the combustion-supporting power assisting device that purifies, burn the pure hydrogen mixed gas of the waste heat system high pressure high-energy fuel after purifying with tail gas in superhigh temperature ultrahigh pressure; (contain and to be the organic wastewater of Gao Hanneng or to contain ability water or bittern or water by aqua; But catalytic degradation producing hydrogen from organic waste water; At present; Alcohol reforming is a kind of reasonable hydrogen manufacturing mode) relate to a kind of high pollution harmful waste liquid and utilize energy resourceization again, be that the purifier that zero-emission purifies is burned in tail gas superhigh temperature super-high-pressure homogenization compression ignite spontaneous combustion detonation fully---burn the economizer that zero-emission purifies fully with what the organic liquid waste of the highly enriched Gao Hanneng of high pollution high toxicity changed into the high pressure alcohol hydrogen combustion-supporting power-assisted of mixed gas high-energy fuel and made that tail gas fires again, particularly relate to the energy-conservation machine main part device of a kind of tail gas super-high-pressure homogenization detonation zero-emission power-assisted.
Background technique
At present, the tail gas of the internal-combustion engine in the existing known technology fires the shortcoming of the energy-conservation machine of purification again and is: energy-saving effect is lower.Therefore, the launch products of the high energy-conservation little discharging of utmost point needs on the market.
Summary of the invention
At present; Employing with the highly enriched height of high pollution high toxicity contain can organic liquid waste as the energy resource utilization, with the UTILIZATION OF VESIDUAL HEAT IN of motor exhaust with the agent of water alcohol be heated to be make behind the fuel fume waste heat system high pressure alcohol hydrogen mixed gas high-energy fuel of tail gas after the strengening burning of superhigh temperature ultrahigh pressure purifies give the engine combustion-supporting power-assisted (to contain the ability aqua can be the organic wastewater of Gao Hanneng or contain ability water or bittern or water; But catalytic degradation producing hydrogen from organic waste water; At present; Alcohol reforming is a kind of reasonable hydrogen manufacturing mode), be a kind ofly the homogeneous compression-ignition spontaneous combustion detonation in hyperpressure hyperthermal of organic liquid waste, tail gas to be burned fully purify the back and make organic liquid waste be converted into the energy-conservation device of the combustion-supporting power-assisted of high-energy fuel (can save fuel oil 5%～65%)---the technology of the energy-conservation machine main part device of tail gas super-high-pressure homogenization detonation zero-emission power-assisted; That puts down in writing in the document is less, does not up to the present have the sales promotion in enormous quantities of this type of technological product to use on the market as yet.
The objective of the invention is: provide a kind of tail gas super-high-pressure homogenization detonation zero-emission power-assisted energy-conservation machine main part device.
In order to reach above-mentioned purpose; Technological scheme of the present invention is: high-pressure water alcohol combustion agent is set on ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder sprays automatical control system; In water alcohol agent jar, the agent of water alcohol is set; Residual air follower, water alcohol agent cat reformer, water alcohol agent catalytic reforming heating pipe line, superpressure pump after between water alcohol agent jar and the ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder tail gas homogeneous compression-ignition spontaneous combustion detonation being set; Super high pressure-charging turbocharger, pure hydrogen mixed gas generator are set on tail pipe; Between tail pipe and ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder, super high pressure-charging tail gas loader is set; Water alcohol agent catalytic reforming heating pipe line is set in water alcohol agent cat reformer, pure hydrogen mixed gas generation catalyzer, engine high pressure alcohol hydrogen mixed gas fuel air pipe are set on pure hydrogen mixed gas generator.The high flame ignition device of superhigh temperature, high-pressure water alcohol combustion agent high temperature heated capillary again is set on ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder; Trunnion, high oxygen-enriched air loader, super high pressure-charging tail gas pulse input automatical control system are set between tail pipe and ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder; High-pressure water alcohol agent pipeline is set between water alcohol agent catalytic reforming heating pipe line and superpressure pump; High-pressure water alcohol combustion agent pipeline is set between water alcohol agent catalytic reforming heating pipe line and pure hydrogen mixed gas generator, on pure hydrogen mixed gas generator, temperature controller is set.Low-temp tail gas purifier, purifying carbon dioxide device are set on tail pipe; High-pressure water alcohol agent output control system is set between high-pressure water alcohol agent pipeline and superpressure pump; Between heated capillary and the water alcohol agent catalytic reforming heating pipe line high-pressure water alcohol is set again at high-pressure water alcohol combustion agent high temperature and fires agent homogeneous detonation output system; Between water alcohol agent catalytic reforming heating pipe line and high-pressure water alcohol combustion agent pipeline, a large amount of output systems of high-pressure water alcohol combustion agent are set; High pressure alcohol hydrogen mixed gas set out motivation output tube, high pressure alcohol hydrogen mixed gas output control system are set between pure hydrogen mixed gas generator and engine high pressure alcohol hydrogen mixed gas fuel air pipe; Between high pressure alcohol hydrogen mixed gas is seted out motivation output tube and high pressure alcohol hydrogen mixed gas output control system, the pure hydrogen mixed gas of high pressure basin is set; The low-temp tail gas cleaning catalyst is set in the low-temp tail gas purifier, the purifying carbon dioxide catalyzer is set in the purifying carbon dioxide device.One end of superpressure pump is connected UNICOM's the other end and is connected UNICOM with water alcohol agent catalytic reforming heating pipe line with water alcohol agent jar; An end of residual air follower is connected UNICOM's the other end and is connected UNICOM with water alcohol agent cat reformer after the tail gas homogeneous compression-ignition spontaneous combustion detonation with ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder; One end of alcohol hydrogen mixed gas generator is connected UNICOM's the other end with engine high pressure alcohol hydrogen mixed gas fuel air pipe and is connected with water alcohol agent catalytic reforming heating pipe line; The end that automatical control system is sprayed in high-pressure water alcohol combustion agent is connected UNICOM with water alcohol agent catalytic reforming heating pipe line; One end of super high pressure-charging tail gas loader is connected UNICOM's the other end and is connected UNICOM with ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder with tail pipe, an end of tail pipe is connected UNICOM's the other end and is connected UNICOM with super high pressure-charging tail gas loader with the super high pressure-charging turbocharger.A high-pressure water alcohol combustion agent high temperature end and the high-pressure water alcohol combustion agent of heated capillary again sprays automatical control system and is connected UNICOM's the other end and is connected UNICOM with the pure agent catalytic reforming of water heating pipe line; One end of trunnion is connected UNICOM's the other end and is connected UNICOM with ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder with tail pipe; One end of high oxygen-enriched air loader is connected UNICOM with trunnion; One end of high-pressure water alcohol agent pipeline is connected UNICOM's the other end with water alcohol agent catalytic reforming heating pipe line and is connected UNICOM with superpressure pump; One end of high-pressure water alcohol combustion agent pipeline is connected UNICOM's the other end with water alcohol agent catalytic reforming heating pipe line and is connected UNICOM with pure hydrogen mixed gas generator; One end of temperature controller is connected with pure hydrogen mixed gas generator, and an end of super high pressure-charging tail gas pulse input automatical control system is connected UNICOM's the other end and is connected UNICOM with ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder with super high pressure-charging tail gas loader.Be connected UNICOM's the other end with superpressure pump at an end of high-pressure water alcohol agent output control system and be connected UNICOM with the pure agent pipeline of high-pressure water; One end of high-pressure water alcohol combustion agent homogeneous detonation output system and high-pressure water alcohol combustion agent high temperature heated capillary again are connected UNICOM's the other end and are connected UNICOM with the pure agent catalytic reforming of water heating pipe line, the pure a large amount of output systems of agent of firing of high-pressure water; One end of a large amount of output systems of high-pressure water alcohol combustion agent is connected UNICOM's the other end and is connected UNICOM with water alcohol agent catalytic reforming heating pipe line, high-pressure water alcohol combustion agent homogeneous detonation output system with high-pressure water alcohol combustion agent pipeline; A set out end of motivation output tube of high pressure alcohol hydrogen mixed gas is connected UNICOM's the other end and is connected UNICOM with the pure hydrogen mixed gas of high pressure basin with pure hydrogen mixed gas generator; One end of high pressure alcohol hydrogen mixed gas output control system is connected UNICOM's the other end with high pressure alcohol hydrogen mixed gas basin and is connected UNICOM with the pure hydrogen mixed gas of engine high pressure fuel air pipe, and automatical control system, the ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder UNICOM that is linked in sequence is imported in super high pressure-charging turbocharger, tail pipe, low-temp tail gas purifier, purifying carbon dioxide device, trunnion, super high pressure-charging tail gas loader, the pulse of super high pressure-charging tail gas.
The invention has the beneficial effects as follows: 1, simple in structure, 2, practicability is stronger, 3, stable performance, 4, energy-conservation combustion-supporting power-assisted, 5, the harmful substance high speed purifying utilizes, 6, the environmental protection zero-emission, 7, be convenient to apply fast.
Description of drawings
Below in conjunction with accompanying drawing and embodiment the present invention is further described.
Fig. 1 is the brief introduction schematic representation of the energy-conservation machine main part device of tail gas super-high-pressure homogenization detonation zero-emission power-assisted of the present invention embodiment's working principle.
Among the figure: 1, tail gas supplying tube, 2, high-temperature tail gas, 3, the super high pressure-charging turbocharger, 4, tail pipe; 5, low-temp tail gas purifier, 6, the low-temp tail gas cleaning catalyst, 7, the purifying carbon dioxide device, 8, the purifying carbon dioxide catalyzer; 9, trunnion, 10, high oxygen-enriched air loader, 11, super high pressure-charging tail gas loader, 12, ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder; 13, super high pressure-charging tail gas pulse input automatical control system, 14, high-pressure water alcohol combustion agent sprays automatical control system, 15, high-pressure water alcohol combustion agent high temperature heated capillary again, 16, high-pressure water alcohol agent output control system; 17, superpressure pump, 18, water alcohol agent jar, 19, the agent of water alcohol, 20, residual air follower after the tail gas homogeneous compression-ignition spontaneous combustion detonation; 21, water alcohol agent cat reformer, 22, water alcohol agent catalytic reforming heating pipe line, 23, high-pressure water alcohol combustion agent homogeneous detonation output system, 24, high-pressure water alcohol combustion agent pipeline; 25, high-pressure water alcohol agent pipeline, 26, a large amount of output systems of high-pressure water alcohol combustion agent, 27, pure hydrogen mixed gas generator; 28, pure hydrogen mixed gas generation catalyzer, 29, temperature controller, 30, the high pressure alcohol hydrogen mixed gas motivation output tube of setting out; 31, high pressure alcohol hydrogen mixed gas basin, 32, high pressure alcohol hydrogen mixed gas output control system, 33, engine high pressure alcohol hydrogen mixed gas fuel air pipe; 34, the detonation of tail gas homogeneous purifies back residual air discharge pipe, and 35, clean air, 36, the high flame ignition device of superhigh temperature.
Embodiment
In Fig. 1; This device is contained the highly enriched height of high pollution high toxicity organic liquid waste water alcohol agent heating to make fuel vapor system by the using waste heat from tail gas utilization; UTILIZATION OF VESIDUAL HEAT IN low-temp tail gas catalytic purification carbon dioxide multiple-effect composite catalyzing purifies the complete incinerating and purifying system of superhigh temperature super-high-pressure homogenization compression ignite spontaneous combustion detonation, and the combustion-supporting force aid system of economizer (can save fuel oil 5%～65%) the 3 big systems that UTILIZATION OF VESIDUAL HEAT IN water alcohol combustion agent system high pressure alcohol hydrogen mixed gas high-energy fuel improves engine power form.The 1st system is by the agent (19) of water alcohol; Water alcohol agent jar (18); Superpressure pump (17); High-pressure water alcohol agent output control system (16); High-pressure water alcohol agent pipeline (25); Water alcohol agent cat reformer (21); Water alcohol agent catalytic reforming heating pipe line (22); High-pressure water alcohol combustion agent homogeneous detonation output system (23); Ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12); Residual air follower (20) after the tail gas homogeneous compression-ignition spontaneous combustion detonation; High-pressure water alcohol combustion agent high temperature is heated capillary (15) again; Automatical control system (14) is sprayed in high-pressure water alcohol combustion agent; The high flame ignition device of superhigh temperature (36); Super high pressure-charging tail gas pulse input automatical control system (13); Super high pressure-charging tail gas loader (11); High oxygen-enriched air loader (10); Trunnion (9); Tail pipe (4); Super high pressure-charging turbocharger (3); The detonation of tail gas homogeneous purifies back residual air discharge pipe (34) and forms.The 2nd system is by tail gas supplying tube (1); High-temperature tail gas (2); Super high pressure-charging turbocharger (3); Tail pipe (4); Low-temp tail gas purifier (5); Low-temp tail gas cleaning catalyst (6); Purifying carbon dioxide device (7); Purifying carbon dioxide catalyzer (8); Trunnion (9); High oxygen-enriched air loader (10); Super high pressure-charging tail gas loader (11); Super high pressure-charging tail gas pulse input automatical control system (13); Ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12); The high flame ignition device of superhigh temperature (36); Automatical control system (14) is sprayed in high-pressure water alcohol combustion agent; High-pressure water alcohol combustion agent high temperature is heated capillary (15) again; Residual air follower (20) after the tail gas homogeneous compression-ignition spontaneous combustion detonation; High-pressure water alcohol combustion agent homogeneous detonation output system (23); Water alcohol agent cat reformer (21); Water alcohol agent catalytic reforming heating pipe line (22); High-pressure water alcohol agent pipeline (25); The detonation of tail gas homogeneous purifies back residual air discharge pipe (34) and forms.The 3rd system is by tail gas supplying tube (1); High-temperature tail gas (2); Super high pressure-charging turbocharger (3); Tail pipe (4); Low-temp tail gas purifier (5); Low-temp tail gas cleaning catalyst (6); Purifying carbon dioxide device (7); Purifying carbon dioxide catalyzer (8); Trunnion (9); High oxygen-enriched air loader (10); Super high pressure-charging tail gas loader (11); Super high pressure-charging tail gas pulse input automatical control system (13); Ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12); Automatical control system (14) is sprayed in high-pressure water alcohol combustion agent; High-pressure water alcohol combustion agent high temperature is heated capillary (15) again; The high flame ignition device of superhigh temperature (36); Residual air follower (20) after the tail gas homogeneous compression-ignition spontaneous combustion detonation; High-pressure water alcohol combustion agent homogeneous detonation output system (23); Water alcohol agent cat reformer (21); Water alcohol agent catalytic reforming heating pipe line (22); High-pressure water alcohol agent pipeline (25); The high-pressure water alcohol combustion a large amount of output systems of agent (26); High-pressure water alcohol combustion agent pipeline (24); Alcohol hydrogen mixed gas generator (27); Alcohol hydrogen mixed gas generation catalyzer (28); Temperature controller (29); The high pressure alcohol hydrogen mixed gas motivation output tube (30) of setting out; High pressure alcohol hydrogen mixed gas basin (31); High pressure alcohol hydrogen mixed gas output control system (32); Engine high pressure alcohol hydrogen mixed gas fuel air pipe (33); The detonation of tail gas homogeneous purifies back residual air discharge pipe (34) and forms.
Water alcohol agent jar (18), superpressure pump (17), high-pressure water alcohol agent output control system (16), high-pressure water alcohol agent pipeline (25), water alcohol agent catalytic reforming heating pipe line (22), high-pressure water alcohol combustion agent homogeneous detonation output system (23), high-pressure water alcohol combustion agent high temperature heated capillary (15), high-pressure water alcohol combustion agent again spray automatical control system (14) and are linked in sequence, and the agent (19) of water alcohol is set in water alcohol agent jar (18).Ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) by super high pressure-charging tail gas pulse input automatical control system (13), super high pressure-charging tail gas loader (11), tail gas homogeneous compression-ignition spontaneous combustion detonation after residual air follower (20), water alcohol agent cat reformer (21), high-pressure water alcohol combustion agent spray automatical control system (14), form again by heated capillary (15), the high flame ignition device of superhigh temperature (36) for high-pressure water alcohol combustion agent high temperature; The high flame ignition device of superhigh temperature (36), high-pressure water alcohol combustion agent injection automatical control system (14), high-pressure water alcohol combustion agent high temperature heated capillary (15) again is set on ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12), and high-pressure water alcohol combustion agent injection automatical control system (14), high-pressure water alcohol combustion agent high temperature heated capillary (15), high-pressure water alcohol combustion agent homogeneous detonation output system (23), the pure agent catalytic reforming heating pipe line (22) of water, high-pressure water alcohol agent pipeline (25), high-pressure water alcohol agent output control system (16), superpressure pump (17), water alcohol agent jar (18) again are linked in sequence.Ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) external be provided with connect water alcohol agent cat reformer (21), the detonation of tail gas homogeneous to purify back residual air discharge pipe (34), tail gas homogeneous compression-ignition spontaneous combustion detonation after residual air follower (20), super high pressure-charging tail gas pulse input automatical control system (13), super high pressure-charging tail gas loader (11), trunnion (9), high oxygen-enriched air loader (10), tail pipe (4), super high pressure-charging turbocharger (3).One end of superpressure pump (17) is connected the other end and is connected with high-pressure water alcohol agent output control system (16) with water alcohol agent jar (18); One end of high-pressure water alcohol agent pipeline (25) is connected the other end and is connected with water alcohol agent catalytic reforming heating pipe line (22) with high-pressure water alcohol agent output control system (16), the end that high-pressure water alcohol fires agent homogeneous detonation output system (23) be connected with the pure agent catalytic reforming heating pipe line of water (22) the other end and high-pressure water pure fire agent high temperature again heated capillary (15) be connected.Residual air follower (20) was connected after one end of water alcohol agent cat reformer (21) and the detonation of tail gas homogeneous purified back residual air discharge pipe (34) and be connected the other end and tail gas homogeneous compression-ignition spontaneous combustion detonation, and the pure agent catalytic reforming heating pipe line (22) of water is set in the pure agent cat reformer of water (21).One end of super high pressure-charging tail gas loader (11) and the pulse of super high pressure-charging tail gas input automatical control system (13), ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) are connected the other end and are connected with trunnion (9), tail pipe (4), super high pressure-charging turbocharger (3), and a high-pressure water alcohol combustion agent high temperature end and the high-pressure water alcohol of heated capillary (15) again fires agent injection automatical control system (14) and is connected the other end and is connected with the pure agent homogeneous detonation output system (23) of firing of high-pressure water.One end of super high pressure-charging tail gas pulse input automatical control system (13) is connected the other end and is connected with ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) with super high pressure-charging tail gas loader (11), super high pressure-charging turbocharger (3), tail pipe (4), low-temp tail gas purifier (5), purifying carbon dioxide device (7), trunnion (9), super high pressure-charging tail gas loader (11), super high pressure-charging tail gas pulse input automatical control system (13), ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) are linked in sequence.
Tail gas supplying tube (1), super high pressure-charging turbocharger (3), tail pipe (4), low-temp tail gas purifier (5), purifying carbon dioxide device (7), trunnion (9), super high pressure-charging tail gas loader (11), super high pressure-charging tail gas pulse input automatical control system (13), ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) are linked in sequence, ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) by super high pressure-charging tail gas pulse input automatical control system (13), super high pressure-charging tail gas loader (11), tail gas homogeneous compression-ignition spontaneous combustion detonation after residual air follower (20), water alcohol agent cat reformer (21), high-pressure water alcohol combustion agent spray automatical control system (14), form again by heated capillary (15), the high flame ignition device of superhigh temperature (36) for high-pressure water alcohol combustion agent high temperature.The high flame ignition device of superhigh temperature (36), high-pressure water alcohol combustion agent injection automatical control system (14), high-pressure water alcohol combustion agent high temperature heated capillary (15) again is set on ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12), and high-pressure water alcohol combustion agent injection automatical control system (14), high-pressure water alcohol combustion agent high temperature heated capillary (15), high-pressure water alcohol combustion agent homogeneous detonation output system (23), the pure agent catalytic reforming heating pipe line (22) of water, high-pressure water alcohol agent pipeline (25) again are linked in sequence.External setting the at ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) connects water alcohol agent cat reformer (21); The detonation of tail gas homogeneous purifies back residual air discharge pipe (34); Residual air follower (20) after the tail gas homogeneous compression-ignition spontaneous combustion detonation; Super high pressure-charging tail gas pulse input automatical control system (13); Super high pressure-charging tail gas loader (11); Trunnion (9); High oxygen-enriched air loader (10); Tail pipe (4); Purifying carbon dioxide device (7); Low-temp tail gas purifier (5); Super high pressure-charging turbocharger (3).One end of water alcohol agent catalytic reforming heating pipe line (22) is connected the other end and is connected with high-pressure water alcohol combustion agent homogeneous detonation output system (23) with high-pressure water alcohol agent pipeline (25); A high-pressure water alcohol combustion agent high temperature end of heated capillary (15) again is connected the other end and is connected with the pure agent injection automatical control system (14) that fires of high-pressure water with high-pressure water alcohol combustion agent homogeneous detonation output system (23); After one end of water alcohol agent cat reformer (21) and the tail gas homogeneous compression-ignition spontaneous combustion detonation residual air follower (20) is connected the other end and tail gas homogeneous detonation purification afterwards residual air discharge pipe (34) be connected; Water alcohol agent catalytic reforming heating pipe line (22) is set in water alcohol agent cat reformer (21); One end of trunnion (9) is connected the other end and is connected with tail pipe (4) with super high pressure-charging tail gas loader (11), super high pressure-charging tail gas pulse input automatical control system (13); One end of high oxygen-enriched air loader (10) is connected with trunnion (9), and an end of super high pressure-charging turbocharger (3) is connected the other end and is connected with tail gas supplying tube (1) with tail pipe (4).Low-temp tail gas cleaning catalyst (6) is set in low-temp tail gas purifier (5); Purifying carbon dioxide catalyzer (8) is set in purifying carbon dioxide device (7), and an end of super high pressure-charging tail gas pulse input automatical control system (13) is connected the other end and is connected with ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) with super high pressure-charging tail gas loader (11).High-temperature tail gas (2) enters in the body of high-pressure refractory tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) through tail gas supplying tube (1), super high pressure-charging turbocharger (3), tail pipe (4), low-temp tail gas purifier (5), purifying carbon dioxide device (7), trunnion (9), super high pressure-charging tail gas loader (11), super high pressure-charging tail gas pulse input automatical control system (13).
Tail gas supplying tube (1), super high pressure-charging turbocharger (3), tail pipe (4), low-temp tail gas purifier (5), purifying carbon dioxide device (7), trunnion (9), super high pressure-charging tail gas loader (11), super high pressure-charging tail gas pulse input automatical control system (13), ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) are linked in sequence, ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) by super high pressure-charging tail gas pulse input automatical control system (13), super high pressure-charging tail gas loader (11), tail gas homogeneous compression-ignition spontaneous combustion detonation after residual air follower (20), water alcohol agent cat reformer (21), high-pressure water alcohol combustion agent spray automatical control system (14), form again by heated capillary (15), the high flame ignition device of superhigh temperature (36) for high-pressure water alcohol combustion agent high temperature.The high flame ignition device of superhigh temperature (36), high-pressure water alcohol combustion agent injection automatical control system (14), high-pressure water alcohol combustion agent high temperature heated capillary (15) again is set on ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12), and high-pressure water alcohol combustion agent injection automatical control system (14), high-pressure water alcohol combustion agent high temperature heated capillary (15), high-pressure water alcohol combustion agent homogeneous detonation output system (23), the pure agent catalytic reforming heating pipe line (22) of water, high-pressure water alcohol agent pipeline (25) again are linked in sequence.Ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) external be provided with connect water alcohol agent cat reformer (21), the detonation of tail gas homogeneous to purify back residual air discharge pipe (34), tail gas homogeneous compression-ignition spontaneous combustion detonation after residual air follower (20), super high pressure-charging tail gas pulse input automatical control system (13), super high pressure-charging tail gas loader (11), trunnion (9), tail pipe (4), purifying carbon dioxide device (7), low-temp tail gas purifier (5), super high pressure-charging turbocharger (3).Be provided with at an end of water alcohol agent catalytic reforming heating pipe line (22) and connect high-pressure water alcohol combustion agent homogeneous detonation output system (23), high-pressure water alcohol combustion agent high temperature heated capillary (15), high-pressure water alcohol combustion agent are sprayed automatical control system (14) the other end and be provided with and connect the high-pressure water alcohol combustion a large amount of output systems of agent (26), high-pressure water alcohol combustion agent pipeline (24), pure hydrogen mixed gas generator (27) again; Pure hydrogen mixed gas generation catalyzer (28), temperature controller (29) are set on pure hydrogen mixed gas generator (27), pure hydrogen mixed gas generation catalyzer (28) is set in pure hydrogen mixed gas generator (27).One end of high pressure alcohol hydrogen mixed gas output control system (32) is connected the other end and is connected with high pressure alcohol hydrogen mixed gas basin (31) with engine high pressure alcohol hydrogen mixed gas fuel air pipe (33); A set out end of motivation output tube (30) of high pressure alcohol hydrogen mixed gas is connected the other end with high pressure alcohol hydrogen mixed gas basin (31) and is connected with pure hydrogen mixed gas generator (27), and the pure end that fires agent pipeline (24) of high-pressure water is connected the other end and is connected with the pure a large amount of output systems of agent (26) of firing of high-pressure water with pure hydrogen mixed gas generator (27).One end of water alcohol agent catalytic reforming heating pipe line (22) is connected the other end and is connected with the high-pressure water alcohol combustion a large amount of output systems of agent (26), high-pressure water alcohol combustion agent homogeneous detonation output system (23) with high-pressure water alcohol agent pipeline (25).One end of super high pressure-charging tail gas pulse input automatical control system (13) is connected the other end and is connected with ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) with super high pressure-charging tail gas loader (11).High-temperature tail gas (2) enters in the body of high-pressure refractory tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) through tail gas supplying tube (1), super high pressure-charging turbocharger (3), tail pipe (4), low-temp tail gas purifier (5), purifying carbon dioxide device (7), trunnion (9), super high pressure-charging tail gas loader (11), super high pressure-charging tail gas pulse input automatical control system (13).Low-temp tail gas cleaning catalyst (6) is set in low-temp tail gas purifier (5); Purifying carbon dioxide catalyzer (8) is set in purifying carbon dioxide device (7); High oxygen-enriched air loader (10) is set on trunnion (9); One end of high oxygen-enriched air loader (10) is connected with trunnion (9), and residual air follower (20) was connected after an end of water alcohol agent cat reformer (21) and the detonation of tail gas homogeneous purified afterwards residual air discharge pipe (34) and be connected the other end and tail gas homogeneous compression-ignition spontaneous combustion detonation.
The workflow of this device: the exhaust outlet end of internal-combustion engine is connected UNICOM with the entrance point of tail gas supplying tube (1); Tail gas supplying tube (1) is connected with tail pipe (4) and is integrated; Between tail gas supplying tube (1) and tail pipe (4), super high pressure-charging turbocharger (3) is set and interconnects UNICOM; Low-temp tail gas purifier (5), purifying carbon dioxide device (7) are set on tail pipe (4); Low-temp tail gas cleaning catalyst (6) is set in low-temp tail gas purifier (5), purifying carbon dioxide catalyzer (8) is set in purifying carbon dioxide device (7).Between tail pipe (4) and super high pressure-charging tail gas loader (11), trunnion (9) is set, high oxygen-enriched air loader (10) is connected UNICOM each other; The pretreated high oxygen-enriched air of a large amount of processes gets into from an end of high oxygen-enriched air loader (10), and an end of high oxygen-enriched air loader (10) is connected UNICOM with trunnion (9).Residual air follower (20) water alcohol agent cat reformer (21) connects each other after super high pressure-charging tail gas loader (11), super high pressure-charging tail gas pulse input automatical control system (13), tail gas homogeneous compression-ignition spontaneous combustion detonation are set on the ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12); Super high pressure-charging tail gas pulse input automatical control system (13) is set, residual air follower (20), water alcohol agent cat reformer (21) UNICOM that is linked in sequence after super high pressure-charging tail gas loader (11), super high pressure-charging tail gas pulse input automatical control system (13), ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12), the tail gas homogeneous compression-ignition spontaneous combustion detonation between super high pressure-charging tail gas loader (11) and ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12).High-pressure water alcohol combustion agent is set on ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) sprays automatical control system (14), high-pressure water alcohol combustion agent high temperature heated capillary (15), the high flame ignition device of superhigh temperature (36) again, residual air discharge pipe (34) was connected UNICOM after residual air follower (20) was connected another outlet end of UNICOM and tail gas homogeneous detonation purification after the entrance point of water alcohol agent cat reformer (21) and the tail gas homogeneous compression-ignition spontaneous combustion detonation.Water alcohol agent catalytic reforming heating pipe line (22) is set in water alcohol agent cat reformer (21); The entrance point of water alcohol agent catalytic reforming heating pipe line (22) is connected another outlet end of UNICOM and is connected UNICOM with high-pressure water alcohol combustion agent homogeneous detonation output system (23), the high-pressure water alcohol combustion a large amount of output systems of agent (26) with high-pressure water alcohol agent pipeline (25), automatical control system (14), high-pressure water alcohol combustion agent high temperature pure agent homogeneous detonation output system (23), the pure agent catalytic reforming heating pipe line (22) of water, the pure agent pipeline of high-pressure water (25) UNICOM that is linked in sequence of firing of heated capillary (15), high-pressure water is again sprayed in high-pressure water alcohol combustion agent.The entrance point of superpressure pump (17) is connected another outlet end of UNICOM and is connected UNICOM with high-pressure water alcohol agent output control system (16), high-pressure water alcohol agent pipeline (25) with water alcohol agent jar (18); High-pressure water alcohol agent pipeline (25), high-pressure water alcohol agent output control system (16), superpressure pump (17), water alcohol agent jar (18) UNICOM that is linked in sequence is provided with the agent (19) of the pretreated water alcohol of many processes in water alcohol agent jar (18).The external pure hydrogen mixed gas generator (27) that is provided with at tail pipe (4); The entrance point of high-pressure water alcohol combustion agent pipeline (24) is connected another outlet end of UNICOM with the high-pressure water alcohol combustion a large amount of output systems of agent (26) and is connected UNICOM with pure hydrogen mixed gas generator (27), and pure hydrogen mixed gas generator (27), high-pressure water alcohol fire the pure a large amount of output systems of agent (26), the pure agent catalytic reforming heating pipe line of water (22) UNICOM that is linked in sequence of firing of agent pipeline (24), high-pressure water.Pure hydrogen mixed gas generation catalyzer (28), temperature controller (29) are set on pure hydrogen mixed gas generator (27); Pure hydrogen mixed gas generation catalyzer (28) is set in pure hydrogen mixed gas generator (27), and an end of temperature controller (29) is connected with pure hydrogen mixed gas generator (27).At the entrance point of high pressure alcohol hydrogen mixed gas basin (31) the high pressure alcohol hydrogen mixed gas motivation output tube (30) of setting out is set and connects that UNICOM's the other end outlet end is provided with high pressure alcohol hydrogen mixed gas output control system (32), engine high pressure alcohol hydrogen mixed gas fuel air pipe (33) connects UNICOM, the entrance point of high pressure alcohol hydrogen mixed gas output control system (32) is connected another outlet end of UNICOM with high pressure alcohol hydrogen mixed gas basin (31) and is connected UNICOM with the pure hydrogen mixed gas fuel air pipe of engine high pressure (33).Alcohol hydrogen mixed gas generator (27), high pressure alcohol hydrogen mixed gas motivation output tube (30), high pressure alcohol hydrogen mixed gas basin (31), high pressure alcohol hydrogen mixed gas output control system (32), engine high pressure alcohol hydrogen mixed gas fuel air pipe (33) UNICOM that is linked in sequence of setting out.High-temperature tail gas (2) enters in the body of high-pressure refractory tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) through tail gas supplying tube (1), super high pressure-charging turbocharger (3), tail pipe (4), low-temp tail gas purifier (5), purifying carbon dioxide device (7), trunnion (9), super high pressure-charging tail gas loader (11), super high pressure-charging tail gas pulse input automatical control system (13); Super high pressure-charging turbocharger (3) is the power source that high-temperature tail gas (2) obtains huge energy, and clean air (35) purifies the back residual air discharge pipe (34) from the detonation of tail gas homogeneous and discharges.
High-temperature tail gas (2) enters in the body of low-temp tail gas purifier (5), purifying carbon dioxide device (7) through tail gas supplying tube (1), super high pressure-charging turbocharger (3), tail pipe (4); Low-temp tail gas cleaning catalyst (6) is set in low-temp tail gas purifier (5); Purifying carbon dioxide catalyzer (8) is set in the body of purifying carbon dioxide device (7), and super high pressure-charging turbocharger (3) is that the high-temperature tail gas (2) of high pressure obtains high-octane maximum power source.The high-temperature tail gas of high pressure (2) purifies the back in the continuous concerted catalysis through low-temp tail gas purifier (5), low-temp tail gas cleaning catalyst (6), purifying carbon dioxide device (7), purifying carbon dioxide catalyzer (8) and enters in the body of super high pressure-charging tail gas loader (11) through trunnion (9), and the pretreated high oxygen-enriched air of a large amount of processes enters in the body of super high pressure-charging tail gas loader (11) through trunnion (9) from high oxygen-enriched air loader (10).High-temperature tail gas of high pressure (2) and high oxygen-enriched air enter into ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) through super high pressure-charging tail gas pulse input automatical control system (13) from super high pressure-charging tail gas loader (11).After the entrance point of water alcohol agent cat reformer (21) and the tail gas homogeneous compression-ignition spontaneous combustion detonation residual air follower (20), ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) is connected another outlet end of UNICOM and tail gas homogeneous detonation purification afterwards residual air discharge pipe (34) be connected UNICOM.Water alcohol agent catalytic reforming heating pipe line (22) is set in the body of water alcohol agent cat reformer (21), and the entrance point of water alcohol agent catalytic reforming heating pipe line (22) is connected another outlet end of UNICOM, and heated capillary (15), high-pressure water alcohol combustion agent are sprayed automatical control system (14) and are connected UNICOM again with high-pressure water alcohol combustion agent homogeneous detonation output system (23), high-pressure water alcohol combustion agent high temperature with high-pressure water alcohol agent pipeline (25), high-pressure water alcohol agent output control system (16), superpressure pump (17).The entrance point of superpressure pump (17) is connected another outlet end of UNICOM and is connected UNICOM with high-pressure water alcohol agent output control system (16), high-pressure water alcohol agent pipeline (25), water alcohol agent catalytic reforming heating pipe line (22) with water alcohol agent jar (18), the agent (19) of the pretreated water alcohol of many processes is set in the body of water alcohol agent jar (18).Water alcohol agent (19) enters into water alcohol agent catalytic reforming heating pipe line (22) through superpressure pump (17), high-pressure water alcohol agent output control system (16), high-pressure water alcohol agent pipeline (25), and heated capillary (15), high-pressure water alcohol combustion agent are sprayed automatical control system (14) and entered into ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) again through high-pressure water alcohol combustion agent homogeneous detonation output system (23), high-pressure water alcohol combustion agent high temperature through changing into high-pressure water alcohol combustion agent behind the catalytic reforming in the water alcohol agent catalytic reforming heating pipe line (22) of the pretreated water alcohol agent of a large amount of processes (19) in water alcohol agent cat reformer (21).High-temperature tail gas (2) behind the continuous catalytic purification of process in the high pressure-temperature and high oxygen-enriched air mix the back and in ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12), mix with high-pressure water alcohol combustion agent, homogeneous compression-ignition spontaneous combustion and pass through the burning completely that the high flame ignition device of superhigh temperature (36) further can carry out the detonation of superfast ultrahigh pressure after the lighting of homogeneous simultaneously again under the high-pressure homogeneous compression of the high pressure piston in ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12).The major function of ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) be the high-temperature tail gas (2) of the high pressure of big flow purify through continuous concerted catalysis the back is mixing with a large amount of high oxygen-enriched air and a spot of high-pressure water alcohol combustion agent the back, high pressure piston further add the high flame ignition device of superhigh temperature (36) again after the homogeneous compression-ignition spontaneous combustion of high pressure compressed simultaneously further after the igniting of high-energy homogeneous, be able to carry out the burning fully completely of detonation of superfast ultrahigh pressure.With transforming into clean air (35) after the purification of burning completely of harmful gas through the superfast superhigh temperature of ultrahigh pressure, purify the back residual air discharge pipe (34) from the detonation of tail gas homogeneous and discharge, can reach the purpose of zero-emission.The clean air of high temperature (35) through tail gas homogeneous compression-ignition spontaneous combustion detonation after residual air follower (20) enter into water alcohol agent cat reformer (21); After water alcohol agent catalytic reforming heating pipe line (22) carried out the catalytic reforming of ultrahigh pressure UTILIZATION OF VESIDUAL HEAT IN; Most high-pressure water alcohol combustion agent wherein enters in the body of pure hydrogen mixed gas generator (27) through the high-pressure water alcohol combustion a large amount of output systems of agent (26), high-pressure water alcohol combustion agent pipeline (24); Pure hydrogen mixed gas generation catalyzer (28), temperature controller (29) are set on pure hydrogen mixed gas generator (27); Pure hydrogen mixed gas generation catalyzer (28) is set in the body of pure hydrogen mixed gas generator (27); The UTILIZATION OF VESIDUAL HEAT IN of high-temperature tail gas (2) in the tail pipe (4); The pure combustion of high-pressure water agent transforms into high pressure alcohol hydrogen mixed gas under the continuous effect of pure hydrogen mixed gas generator (27), pure hydrogen mixed gas generation catalyzer (28), temperature controller (29), from high pressure alcohol hydrogen mixed gas is seted out motivation output tube (30), engine high pressure alcohol hydrogen mixed gas fuel air pipe (33), export.The effect of high pressure alcohol hydrogen mixed gas basin (31), high pressure alcohol hydrogen mixed gas output control system (32) is the pure hydrogen mixed gas fuel with high pressure; According to the reasonably optimally-controlled continuous pulse output of the demand of the reality of internal-combustion engine; Motor is carried out the help that increases substantially power of combustion-supporting power-assisted, may ultimately reach energy-efficient purpose.The high-temperature tail gas of high pressure (2) is behind process low temperature purification catalysis and carbon dioxide process purifying and catalyzing; Under the effect of the huge energy of super high pressure-charging turbocharger (3); With high oxygen-enriched air loader (10) in high oxygen-enriched air mix after; Enter into ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) through super high pressure-charging tail gas loader (11), super high pressure-charging tail gas pulse input automatical control system (13); Further tentatively begin the homogeneous compression-ignition spontaneous combustion under the compression of high pressure again at high pressure piston; At the same time; The high flame ignition device of superhigh temperature (36), high-pressure water alcohol combustion agent high temperature again heated capillary (15), high-pressure water alcohol combustion agent spray carry out under the synchronous synergetic effect of automatical control system (14) superfast ultrahigh pressure [the water alcohol combustion agent of most ultrahigh pressure is that the injection of the preliminary compression ignite involuntary ignition of tail gas after, carrying out ultrahigh pressure again enters into cylinder, and the fire nuclear of many places forms in this moment cylinder, and beginning is with superfast high flame propagation; The detonation of ultrahigh pressure promptly takes place subsequently] detonation burns purification completely, can reach the purpose of zero-emission.
This device is actual be a kind of multiple comprehensive high pollution that is used for bio-refractory highly toxic highly enriched Gao Hanneng organic liquid waste and tail gas efficient zero-emission purifying processing device and UTILIZATION OF VESIDUAL HEAT IN highly toxic organic liquid waste is changed into high pressure alcohol hydrogen mixed gas high-energy fuel carries out combustion-supporting power-assisted to motor energy-efficient apparatus.What it adopted: 1, the using waste heat from tail gas utilization contains the highly enriched height of high pollution high toxicity organic liquid waste water alcohol agent heating to make fuel vapor system; 2, the low-temperature catalyzed purification of the multiple-effect of tail gas, carbon dioxide multiple-effect composite catalyzing purify, superhigh temperature ultra high speed super-high-pressure homogenization compression ignite spontaneous combustion detonation incinerating and purifying system, and 3, UTILIZATION OF VESIDUAL HEAT IN contains the highly enriched height of high pollution high toxicity 3 big systems of the combustion-supporting force aid system of economizer that can organic liquid waste water alcohol vapor system high pressure alcohol hydrogen mixed gas high-energy fuel raising engine power.Adopt purification method that multiple ultrahigh pressure ultra high speed extrahigh energy superhigh temperature homogeneous compression-ignition spontaneous combustion detonation burns fully with purpose of guaranteeing to make tail gas reach zero-emission and the organic liquid waste that adopts UTILIZATION OF VESIDUAL HEAT IN with the highly toxic highly enriched Gao Hanneng of high pollution of bio-refractory, water alcohol vapor system high pressure alcohol hydrogen mixed gas high-energy fuel to motor carry out combustion-supporting power-assisted (can save fuel oil 5%～65%) economizer of smoke consumer be the purifier device of multiple-effect function, be that the purifying processor of a kind of tail gas zero-emission of firing again also can make the organic liquid waste zero-emission purified treatment of the highly enriched Gao Hanneng of high pollution high toxicity and the energy-efficient apparatus of energy resource utilization.Be adapted at using on the common internal combustion engine or on the motor of special use, using.
The working pressure of super high pressure-charging turbocharger (3) is about 0.10～6Mpa (1～60 barometric pressure); The working pressure of ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) is about 1～60Mpa (10～600 barometric pressure), and the working pressure of superpressure pump (17) is about 10～600Mpa (100～6000 barometric pressure).
Claims (6)
1. energy-conservation machine main part device of tail gas super-high-pressure homogenization detonation zero-emission power-assisted; Comprise tail gas supplying tube, low-temp tail gas purifier, tail-gas catalyst, tail gas pipeline, residual air discharge pipe; It is characterized in that: high-pressure water alcohol combustion agent is set on ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) sprays automatical control system (14); The agent (19) of water alcohol is set in water alcohol agent jar (18); Residual air follower (20), water alcohol agent cat reformer (21), water alcohol agent catalytic reforming heating pipe line (22), superpressure pump (17) after between water alcohol agent jar (18) and the ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) tail gas homogeneous compression-ignition spontaneous combustion detonation being set; Super high pressure-charging turbocharger (3), pure hydrogen mixed gas generator (27) are set on tail pipe (4); Between tail pipe (4) and ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12), super high pressure-charging tail gas loader (11) is set; Water alcohol agent catalytic reforming heating pipe line (22) is set in water alcohol agent cat reformer (21), pure hydrogen mixed gas generation catalyzer (28), engine high pressure alcohol hydrogen mixed gas fuel air pipe (33) are set on pure hydrogen mixed gas generator (27).
2. the energy-conservation machine main part device of tail gas super-high-pressure homogenization detonation zero-emission power-assisted according to claim 1; It is characterized in that: the high flame ignition device of superhigh temperature (36), high-pressure water alcohol combustion agent high temperature heated capillary (15) again is set on ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12); Trunnion (9), high oxygen-enriched air loader (10), super high pressure-charging tail gas pulse input automatical control system (13) are set between tail pipe (4) and ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12); High-pressure water alcohol agent pipeline (25) is set between water alcohol agent catalytic reforming heating pipe line (22) and superpressure pump (17); High-pressure water alcohol combustion agent pipeline (24) is set between water alcohol agent catalytic reforming heating pipe line (22) and pure hydrogen mixed gas generator (27), temperature controller (29) is set on pure hydrogen mixed gas generator (27).
3. the energy-conservation machine main part device of tail gas super-high-pressure homogenization detonation zero-emission power-assisted according to claim 1; It is characterized in that: low-temp tail gas purifier (5), purifying carbon dioxide device (7) are set on tail pipe (4); High-pressure water alcohol agent output control system (16) is set between high-pressure water alcohol agent pipeline (25) and superpressure pump (17); Between heated capillary (15) and the water alcohol agent catalytic reforming heating pipe line (22) high-pressure water alcohol is set again at high-pressure water alcohol combustion agent high temperature and fires agent homogeneous detonation output system (23); The high-pressure water alcohol combustion a large amount of output systems of agent (26) are set between water alcohol agent catalytic reforming heating pipe line (22) and high-pressure water alcohol combustion agent pipeline (24); High pressure alcohol hydrogen mixed gas set out motivation output tube (30), high pressure alcohol hydrogen mixed gas output control system (32) are set between pure hydrogen mixed gas generator (27) and engine high pressure alcohol hydrogen mixed gas fuel air pipe (33); Between high pressure alcohol hydrogen mixed gas is seted out motivation output tube (30) and high pressure alcohol hydrogen mixed gas output control system (32), the pure hydrogen mixed gas basin (31) of high pressure is set; Low-temp tail gas cleaning catalyst (6) is set in low-temp tail gas purifier (5), purifying carbon dioxide catalyzer (8) is set in purifying carbon dioxide device (7).
4. the energy-conservation machine main part device of tail gas super-high-pressure homogenization detonation zero-emission power-assisted according to claim 1; It is characterized in that: an end of superpressure pump (17) is connected UNICOM's the other end and is connected UNICOM with water alcohol agent catalytic reforming heating pipe line (22) with water alcohol agent jar (18); An end of residual air follower (20) is connected UNICOM's the other end and is connected UNICOM with water alcohol agent cat reformer (21) after the tail gas homogeneous compression-ignition spontaneous combustion detonation with ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12); One end of alcohol hydrogen mixed gas generator (27) is connected UNICOM's the other end and is connected with water alcohol agent catalytic reforming heating pipe line (22) with engine high pressure alcohol hydrogen mixed gas fuel air pipe (33); The end that automatical control system (14) is sprayed in high-pressure water alcohol combustion agent is connected UNICOM with water alcohol agent catalytic reforming heating pipe line (22); One end of super high pressure-charging tail gas loader (11) is connected UNICOM's the other end and is connected UNICOM with ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) with tail pipe (4), an end of tail pipe (4) is connected UNICOM's the other end and is connected UNICOM with super high pressure-charging tail gas loader (11) with super high pressure-charging turbocharger (3).
5. the energy-conservation machine main part device of tail gas super-high-pressure homogenization detonation zero-emission power-assisted according to claim 1 and 2; It is characterized in that: a high-pressure water alcohol combustion agent high temperature end and the high-pressure water alcohol combustion agent of heated capillary (15) again sprays automatical control system (14) and is connected UNICOM's the other end and is connected UNICOM with the pure agent catalytic reforming heating pipe line of water (22); One end of trunnion (9) is connected UNICOM's the other end and is connected UNICOM with ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) with tail pipe (4); One end of high oxygen-enriched air loader (10) is connected UNICOM with trunnion (9); One end of high-pressure water alcohol agent pipeline (25) is connected UNICOM's the other end with water alcohol agent catalytic reforming heating pipe line (22) and is connected UNICOM with superpressure pump (17); One end of high-pressure water alcohol combustion agent pipeline (24) is connected UNICOM's the other end with water alcohol agent catalytic reforming heating pipe line (22) and is connected UNICOM with pure hydrogen mixed gas generator (27); One end of temperature controller (29) is connected with pure hydrogen mixed gas generator (27), and an end of super high pressure-charging tail gas pulse input automatical control system (13) is connected UNICOM's the other end and is connected UNICOM with ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) with super high pressure-charging tail gas loader (11).
6. according to claim 2 or the energy-conservation machine main part device of 3 described tail gas super-high-pressure homogenization detonation zero-emission power-assisteds; It is characterized in that: be connected UNICOM's the other end with superpressure pump (17) at an end of high-pressure water alcohol agent output control system (16) and be connected UNICOM with the pure agent pipeline of high-pressure water (25); One end of high-pressure water alcohol combustion agent homogeneous detonation output system (23) and high-pressure water alcohol combustion agent high temperature heated capillary (15) again are connected UNICOM's the other end and are connected UNICOM with the pure agent catalytic reforming heating pipe line (22) of water, the pure a large amount of output systems of agent (26) of firing of high-pressure water; One end of the high-pressure water alcohol combustion a large amount of output systems of agent (26) is connected UNICOM's the other end and is connected UNICOM with water alcohol agent catalytic reforming heating pipe line (22), high-pressure water alcohol combustion agent homogeneous detonation output system (23) with high-pressure water alcohol combustion agent pipeline (24); A set out end of motivation output tube (30) of high pressure alcohol hydrogen mixed gas is connected UNICOM's the other end and is connected UNICOM with the pure hydrogen mixed gas basin of high pressure (31) with pure hydrogen mixed gas generator (27); One end of high pressure alcohol hydrogen mixed gas output control system (32) is connected UNICOM's the other end and is connected UNICOM with the pure hydrogen mixed gas fuel air pipe of engine high pressure (33) with high pressure alcohol hydrogen mixed gas basin (31), automatical control system (13), ultrahigh pressure heatproof tail gas homogeneous compression-ignition spontaneous combustion detonation cylinder (12) UNICOM that is linked in sequence is imported in super high pressure-charging turbocharger (3), tail pipe (4), low-temp tail gas purifier (5), purifying carbon dioxide device (7), trunnion (9), super high pressure-charging tail gas loader (11), the pulse of super high pressure-charging tail gas.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010102305650A CN102337986A (en) | 2010-07-19 | 2010-07-19 | Tail gas ultra-high-pressure homogeneous deflagration zero-discharge assisting energy-saving machine main piece device |
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| CN2010102305650A CN102337986A (en) | 2010-07-19 | 2010-07-19 | Tail gas ultra-high-pressure homogeneous deflagration zero-discharge assisting energy-saving machine main piece device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103807130A (en) * | 2013-11-29 | 2014-05-21 | 上海合既得动氢机器有限公司 | Methanol produced hydrogen power pump and driving method thereof |
| CN109469564A (en) * | 2012-03-21 | 2019-03-15 | 玫玛研究有限责任公司 | Use the mixture based on water as the internal combustion engine of fuel and the method for operating it |
-
2010
- 2010-07-19 CN CN2010102305650A patent/CN102337986A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109469564A (en) * | 2012-03-21 | 2019-03-15 | 玫玛研究有限责任公司 | Use the mixture based on water as the internal combustion engine of fuel and the method for operating it |
| CN103807130A (en) * | 2013-11-29 | 2014-05-21 | 上海合既得动氢机器有限公司 | Methanol produced hydrogen power pump and driving method thereof |
| CN103807130B (en) * | 2013-11-29 | 2016-06-29 | 上海合既得动氢机器有限公司 | Alcohol hydrogen kinetic pump and driving method thereof |
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Application publication date: 20120201 |