CN1962558A - System for united electricity generation using coke oven gas, tar oil, flume and producing composite fertilizer - Google Patents
System for united electricity generation using coke oven gas, tar oil, flume and producing composite fertilizer Download PDFInfo
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- CN1962558A CN1962558A CN 200610102161 CN200610102161A CN1962558A CN 1962558 A CN1962558 A CN 1962558A CN 200610102161 CN200610102161 CN 200610102161 CN 200610102161 A CN200610102161 A CN 200610102161A CN 1962558 A CN1962558 A CN 1962558A
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- ammonia
- ammoniacal liquor
- waste heat
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- superheater
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
- Y02E20/18—Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]
Abstract
The invention discloses a coke oven gas, tar, flue gas joint generating and composite fertilizer manufacturing system, which comprises the following parts: fuel gas generating device, by-pass flue gas disposal device, steam engine, three-phase synchronous generator II, ammonia-water steam disposal device, gravity deduster, hot water tank, smoke draining device, second electric three-way valve, double-pressure residual heat furnace and ammonia adsorbing reactor, wherein the double-pressure residual heat furnace is set between first electric three-way valve and second electric three-way valve; the ammonia adsorbing reactor is set between second electric three-way valve and main chimney of smoke draining device.
Description
Technical field
The present invention relates to a kind of system that utilizes coke-oven gas, tar, flue gas combined generating and produce composite chemical fertilizer, it belongs to a kind of coke-oven gas that utilizes purification and becomes diesel oil to make fuel through purifying and catalyzing hydrocracking in tar to generate electricity by the fuel gas generation device and utilize the waste hot steam of fuel gas generation device and coke oven flue gas by waste heat boiler and steam turbine generating and the system that produces the ammonium salt compound chemical fertilizer by the ammoniacal liquor absorption reactor thermally.
Background technology
The power station of China is except utilizing the generating of water power and nuclear power, mainly still based on coal fired power generation now.This coal-fired power plant produces steam by steam boiler and promotes steam turbine and drive generator for electricity generation.Because coal fired power generation will consume a large amount of coal resources and a large amount of dust and the sulfurous gas of discharging, and efficient is low, so it exists, and the consumption coal resources are big, contaminate environment is serious and inefficient shortcoming.In addition, in present coking is produced, produce a large amount of coal gas, tar and high-temperature flue gas, these coal gas, tar and high-temperature flue gas directly do not discharge by just handling, not only contaminate environment but also wasted a large amount of resources.
Summary of the invention
The objective of the invention is to solve existing power generation assembly and exist the system that utilizes coke-oven gas, tar, flue gas combined generating and produce composite chemical fertilizer that coal resources are big, contaminate environment is serious, efficient is low and existing coking production exists the technological difficulties of contaminate environment, waste ample resources and provide a kind of turns bane into boon, turns waste into wealth that consumes.
The present invention addresses the above problem the technical scheme that adopts to be: utilize coke-oven gas, tar, flue gas combined generating and the system that produces composite chemical fertilizer, it comprises one by air filter, first sound damper, air compressor, the coke-oven gas regulator, gas valve, gas filter drain cock, the tar treatment unit, fuel valve, oil fuel purifier, gas-turbine combustion chamber, internal combustion turbine, the fuel gas generation device that wheel box and three-phase synchronous generator I form, a bypass flue gas processing device of forming by the bypass chimney and second sound damper that connects with first electric T-shaped valve, a steam turbine, a three-phase synchronous generator II who is connected with steam turbine, one is arranged on steam turbine low temperature ammonia---ammonia between steam outlet and the import of two pressure waste heat boiler ammoniacal liquor---steam-treated device, a gravity type boat davit fly-ash separator that is contained in the coke oven flue gas insulating pipe, a hot water that connects with the ammoniacal liquor absorption reactor thermally, a fume extractor and second electric T-shaped valve of forming by main chimney and the 3rd sound damper, two pressure waste heat boilers of wherein: it comprises that also can produce a high pressure ammonia---water vapor and low pressure ammonia---water vapor, two pressure waste heat boilers are located between first electric T-shaped valve and second electric T-shaped valve, secondary high temperature superheater in two pressure waste heat boilers connects with the admission end of steam turbine, a superheater in two pressure waste heat boilers connects with the low pressure heating network, and the ammoniacal liquor pump outlet of giving of the ammoniacal liquor import and ammonia of the economizer in two pressure waste heat boilers---steam-treated device connects; And an ammoniacal liquor absorption reactor thermally of producing composite chemical fertilizer, the ammoniacal liquor absorption reactor thermally is arranged between the main chimney in second electric T-shaped valve and the fume extractor, and the water outlet of ammoniacal liquor absorption reactor thermally connects with hot water by hot water valve.
Described pair of pressure waste heat boiler is by the secondary high temperature superheater, a superheater, extended surface tube beam evaporation device and economizer constitute, economizer is contained in two pressure waste heat boiler temperature least significant ends, the ammoniacal liquor import and the ammonia of economizer---connecting in the steam-treated device to aqua ammonia pump, extended surface tube beam evaporation device is arranged on economizer back and coupled, superheater is arranged on the back of extended surface tube beam evaporation device and coupled, the outlet of the low pressure ammonia of a superheater---water vapor connects with the low pressure heating network, the secondary high temperature superheater is contained in two pressure waste heat boiler temperature most significant ends and low pressure ammonia---the import of water vapor is connected with another outlet of a superheater, and the outlet of the high pressure ammonia of secondary high temperature superheater---water vapor connects with the admission end of steam turbine; In extended surface tube beam evaporation device and economizer, identical multi-functional compound working medium is housed.
Described multi-functional compound working medium is made up of ammonia, water and tertiary sodium phosphate, earlier with ammonia and water with ammonia: water=25～28: 100 weight ratio is mixed with ammoniacal liquor, and then again with tertiary sodium phosphate: ammoniacal liquor=weight ratio of 10: 100 is mixed with the multi-functional compound working medium of PH10～11.
Because the present invention has adopted technique scheme, therefore, compares with background technology, has following advantage:
1, comprehensive utilization ratio height.Not only make full use of the generating of coke-oven gas and tar, but also utilize generating waste-heat and coke oven flue gas to generate electricity again, and, the comprehensive utilization ratio of coking is improved, turn bane into boon, turn waste into wealth for heating network provides thermal source, produces the ammonium salt compound chemical fertilizer.
2, improved generating efficiency.Apparatus of the present invention can improve generating efficiency 12% than conventional combined cycle, make thermo-efficiency up to 80%.
3, anticorrosion, the scale inhibition of multi-functional compound working medium energy of the present invention reduces hear rate, improves power generation capacity.Strong to waste heat adaptability, widen the UTILIZATION OF VESIDUAL HEAT IN scope, waste heat all can utilize generating more than 100 ℃.
Description of drawings
Accompanying drawing is a structural representation of the present invention.
Embodiment
The present invention is described in further detail below in conjunction with drawings and Examples.
As shown in drawings, utilize coke-oven gas in the present embodiment, tar, flue gas combined generating and the system that produces composite chemical fertilizer, it comprises one by air filter 2, first sound damper 3, air compressor 4, coke-oven gas regulator 6, gas valve 7, gas filter drain cock 8, tar treatment unit 10, fuel valve 11, oil fuel purifier 12, gas-turbine combustion chamber 13, internal combustion turbine 14, the fuel gas generation device that wheel box 15 and three-phase synchronous generator I16 form, a bypass flue gas processing device of forming by the bypass chimney 21 and second sound damper 20 that connects with first electric T-shaped valve 19, a steam turbine 34, a three-phase synchronous generator II35 who is connected with steam turbine 34, one is arranged on steam turbine 34 low temperature ammonia---ammonia between steam outlet and the 22 ammoniacal liquor imports of two pressure waste heat boiler---steam-treated device, a gravity type boat davit fly-ash separator 18 that is contained in the coke oven flue gas insulating pipe 17, gravity type boat davit fly-ash separator 18 connects with the import of first electric T-shaped valve 19 by coke oven flue gas insulating pipe 17, a hot water 50 that connects with ammoniacal liquor absorption reactor thermally 30 by hot water valve 49, a fume extractor and second electric T-shaped valve 29 of forming by main chimney 32 and the 3rd sound damper 31, two pressure waste heat boilers 22 of wherein: it comprises that also can produce a high pressure ammonia---water vapor and low pressure ammonia---water vapor, two pressure waste heat boilers 22 are located between first electric T-shaped valve 19 and second electric T-shaped valve 29, the inlet mouth of two pressure waste heat boilers 22 connects with an air outlet of first electric T-shaped valve 19, secondary high temperature superheater 23 in two pressure waste heat boilers 22 connects with the admission end of steam turbine 34 by Pressure Steam Valve 33 and high pressure insulating pipe 54, a superheater 24 in two pressure waste heat boilers 22 connects with low pressure heating network 45, and the outlet of giving aqua ammonia pump 43 of the ammoniacal liquor import and ammonia of the economizer 28 in two pressure waste heat boilers 22---steam-treated device connects; And an ammoniacal liquor absorption reactor thermally 30 of producing composite chemical fertilizer, ammoniacal liquor absorption reactor thermally 30 is arranged between the main chimney 32 in second electric T-shaped valve 29 and the fume extractor, and the water outlet of ammoniacal liquor absorption reactor thermally 30 connects with hot water 50 by hot water valve 49; The inlet mouth of ammoniacal liquor absorption reactor thermally 30 connects with an air outlet of second electric T-shaped valve 29, the air outlet of ammoniacal liquor absorption reactor thermally 30 connects with the mouth that advances of main chimney 32, ammoniacal liquor valve 52 be arranged on ammoniacal liquor absorption reactor thermally 30 above, cold valves 48 and ammonium salt compound liquid bleed valve 53 be arranged on ammoniacal liquor absorption reactor thermally 30 below.Hot water feed water valve 51 is located at the side of hot water 50 so that be heat supply grid heat supply water.
As shown in drawings, above-mentioned pair of pressure waste heat boiler 22 is by secondary high temperature superheater 23, a superheater 24, some extended surface tube beam evaporation devices 26 and economizer 28 constitute, economizer 28 is contained in two pressure waste heat boiler 22 temperature least significant ends, the ammoniacal liquor import and the ammonia of economizer 28---the aqua ammonia pump 43 of giving in the steam-treated device connects, some extended surface tube beam evaporation devices 26 are by connection pipe 25,27 link together, some extended surface tube beam evaporation devices 26 are arranged on economizer 28 back and coupled, superheater 24 is arranged on the back of some extended surface tube beam evaporation devices 26 and coupled, the outlet of the low pressure ammonia of a superheater 24---water vapor connects with low pressure heating network 45 by low-pressure steam valve 44, secondary high temperature superheater 23 is contained in two pressure waste heat boiler 22 temperature most significant ends and low pressure ammonia---the import of water vapor is connected with another outlet of a superheater 24, and the outlet of the high pressure ammonia of secondary high temperature superheater 23---water vapor connects with the admission end of steam turbine 34; In some extended surface tube beam evaporation devices 26 and economizer 28, identical multi-functional compound working medium is housed.
As shown in drawings, above-mentioned ammonia---steam-treated device is by direct air-cooled condenser 36, cold blast engine 38, the ammoniacal liquor collector 37 that condenses, the ammoniacal liquor case 39 that condenses, the aqua ammonia pump 40 that condenses, hydrazine (N
2H
4) deoxygenator 41, deoxygenation ammoniacal liquor case 42 and form for aqua ammonia pump 43, directly air-cooled condenser 36 is arranged on steam turbine 34 low temperature ammonia---steam outlet and condensing between the ammoniacal liquor collector 37, directly low temperature ammonia---steam outlet connects with steam turbine 34 in the import of air-cooled condenser 36, and directly the outlet of air-cooled condenser 36 is connected with the ammoniacal liquor collector 37 that condenses; Cold blast engine 38 is contained in one side of direct air-cooled condenser 36, and the import of the ammoniacal liquor case 39 that condenses connects with the ammoniacal liquor collector 37 that condenses, and the outlet of the ammoniacal liquor case 39 that condenses is by aqua ammonia pump 40 and pipeline and the hydrazine (N of condensing
2H
4) import of deoxygenator 41 connects hydrazine (N
2H
4) outlet of deoxygenator 41 connects with the import of deoxygenation ammoniacal liquor case 42, the outlet of deoxygenation ammoniacal liquor case 42 links with the import of giving aqua ammonia pump 43, and the ammoniacal liquor import of the economizer 28 in the outlet of giving aqua ammonia pump 43 and pair pressure waste heat boilers 22 connects.Directly the import of air-cooled condenser 36 also connects with the ammonia water pipe 46 that condenses of heat supplying loop.
For guaranteeing safety, on high pressure insulating pipe 54, be provided with emergency bypass, this emergency bypass is made of safety valve 47 and by-pass line 55, one end of safety valve 47 connects with high pressure insulating pipe 54, the other end of safety valve 47 connects with by-pass line 55, and the other end of by-pass line 55 connects with the ammoniacal liquor import of economizer 28.
The above-mentioned multi-functional compound working medium that is contained in some extended surface tube beam evaporation devices 26 and the economizer 28 is made up of ammonia, water and tertiary sodium phosphate, earlier with ammonia and water with ammonia: the weight ratio of water=25: 100 is mixed with ammoniacal liquor, and then again with tertiary sodium phosphate: ammoniacal liquor=weight ratio of 10: 100 is mixed with the multi-functional compound working medium of PH10～11.Derust and decompose and mend the ammonia effect for improving deoxygenation, can in above-mentioned working medium, add excessive hydrazine (N
2H
4), excessive hydrazine (N
2H
4) the required hydrazine (N that calculates by following reaction formula of add-on
2H
4) amount increase by 20% again.Hydrazine (N
2H
4) reaction formula of deoxygenation is:
N
2H
4+O
2→N
2+2H
2O。
The weight ratio of above-mentioned ammonia and water can also be at ammonia: water=25～28: choose between 100.
Working process of the present invention is: as shown in drawings, with coke-oven gas 5 and tar 9 send into respectively handle in coke-oven gas treatment unit 6 and the tar treatment unit 10 after, enter burning in the gas-turbine combustion chamber 13 by gas valve 7, gas filter drain cock 8 and fuel valve 11, oil fuel purifier 12, the high-temperature fuel gas that produces drives internal combustion turbine 14 work, and drives three-phase synchronous generator I16 generating by wheel box 15.The high-temp waste gas of from internal combustion turbine 14, discharging with enter in two pressure waste heat boilers 22 by the coke oven flue gas insulating pipe 17 and first electric T-shaped valve 19 by gravity type boat davit fly-ash separator 18 dust separating coke oven flue gas, pass through secondary high temperature superheater 23, superheater 24, extended surface tube beam evaporation device 26 and an economizer 28 successively; To enter low pressure ammonia---water vapor is heated into high pressure ammonia---the water composite vapor in the secondary high temperature superheater 23 when high-temp waste gas and coke oven flue gas process secondary high temperature superheater 23, this high pressure ammonia---water composite vapor enters in the steam turbine 34 by Pressure Steam Valve 33 and high pressure insulating pipe 54, promote steam turbine 34 work and drive three-phase synchronous generator II35 generating, steam outlet enters by direct air-cooled condenser 36 high pressure ammonia---the water composite vapor is lowered the temperature after the low temperature ammonia of steam turbine 34---of process work, cold blast engine 38, ammoniacal liquor collector 37 condenses, ammoniacal liquor case 39 condenses, aqua ammonia pump 40 condenses, hydrazine (N
2H
4) deoxygenator 41, deoxygenation ammoniacal liquor case 42 and the ammonia of forming for aqua ammonia pump 43---in the steam-treated device, through ammonia---the ammoniacal liquor that the steam-treated device is handled enters next cycle operation again by entering to aqua ammonia pump 43 in the economizer 28 in two pressure waste heat boilers 22.High-temp waste gas and coke oven flue gas will enter the ammonia vapor in the superheater 24 during through a superheater 24 and be heated into low pressure ammonia---the water composite vapor, the part of this low pressure ammonia---water composite vapor provides thermal source by low-pressure steam valve 44 for low pressure heating network 45, and another part enters in the secondary high temperature superheater 23 so that be heated into high pressure ammonia---and the water composite vapor is generated electricity.To be contained in the ammoniacal liquor complex media heating that the working medium in extended surface tube beam evaporation device 26 and the economizer 28 is made up of ammonia, water and tertiary sodium phosphate when high-temp waste gas and some extended surface tube beam evaporation devices 26 of coke oven flue gas process and economizer 28, make the ammoniacal liquor in the working medium become gaseous state by liquid state, this gaseous state ammoniacal liquor enters in superheater 24 so that be heated into low pressure ammonia---and the water composite vapor is used for low pressure heating network and secondary high temperature superheater 23.Enter the low pressure ammonia in the low pressure heating network 45---water composite vapor cooling back forms condense the condense ammonia water pipe 46 of ammoniacal liquor by heat supplying loop enter ammonia---handling in the steam-treated device,---through ammonia the ammoniacal liquor that the steam-treated device is handled enters next cycle operation.The high-temp waste gas that enters two pressure waste heat boilers 22 and coke oven flue gas become low-temperature flue gas after by above-mentioned heat exchange, and this low-temperature flue gas enters in the ammoniacal liquor absorption reactor thermally 30 by second electric T-shaped valve 29, reacts absorbing carbon dioxide (CO with ammoniacal liquor
2) and sulfurous gas (SO
2), reclaim bicarbonate of ammonia (NH
4HCO
3) and ammonium bisulfite (NH
4HSO
3) waiting the ammonium salt compound chemical fertilizer, low-temperature flue gas is discharged by main chimney 32 after purifying.Enter and become hot water after the cold water heat absorption in the ammoniacal liquor absorption reactor thermally 30 and enter in the hot water 50 by hot water valve 49 and use for hot water pipe net.By hydrazine (N
2H
4) deoxygenator 41 can add excessive hydrazine (N in working medium
2H
4).Among the figure 1 is air.
Claims (3)
1, a kind of coke-oven gas that utilizes, tar, flue gas combined generating and the system that produces composite chemical fertilizer, it comprises one by air filter, first sound damper, air compressor, the coke-oven gas regulator, gas valve, gas filter drain cock, the tar treatment unit, fuel valve, oil fuel purifier, gas-turbine combustion chamber, internal combustion turbine, the fuel gas generation device that wheel box and three-phase synchronous generator I form, a bypass flue gas processing device of forming by the bypass chimney and second sound damper that connects with first electric T-shaped valve, a steam turbine, a three-phase synchronous generator II who is connected with steam turbine, one is arranged on steam turbine low temperature ammonia---ammonia between steam outlet and the import of two pressure waste heat boiler ammoniacal liquor---steam-treated device, a gravity type boat davit fly-ash separator that is contained in the coke oven flue gas insulating pipe, a hot water that connects with the ammoniacal liquor absorption reactor thermally, a fume extractor and second electric T-shaped valve of forming by main chimney and the 3rd sound damper, it is characterized in that: further comprising one and can produce high pressure ammonia two pressure waste heat boilers of---water vapor and low pressure ammonia---water vapor, two pressure waste heat boilers are located between first electric T-shaped valve and second electric T-shaped valve, secondary high temperature superheater in two pressure waste heat boilers connects with the admission end of steam turbine, a superheater in two pressure waste heat boilers connects with the low pressure heating network, and the ammoniacal liquor pump outlet of giving of the ammoniacal liquor import and ammonia of the economizer in two pressure waste heat boilers---steam-treated device connects; And an ammoniacal liquor absorption reactor thermally of producing composite chemical fertilizer, the ammoniacal liquor absorption reactor thermally is arranged between the main chimney in second electric T-shaped valve and the fume extractor, and the water outlet of ammoniacal liquor absorption reactor thermally connects with hot water by hot water valve.
2, a kind of coke-oven gas that utilizes according to claim 1, tar, flue gas combined generating and the system that produces composite chemical fertilizer, it is characterized in that: described pair of pressure waste heat boiler is by the secondary high temperature superheater, a superheater, extended surface tube beam evaporation device and economizer constitute, economizer is contained in two pressure waste heat boiler temperature least significant ends, the ammoniacal liquor import and the ammonia of economizer---connecting in the steam-treated device to aqua ammonia pump, extended surface tube beam evaporation device is arranged on economizer back and coupled, superheater is arranged on the back of extended surface tube beam evaporation device and coupled, the outlet of the low pressure ammonia of a superheater---water vapor connects with the low pressure heating network, the secondary high temperature superheater is contained in two pressure waste heat boiler temperature most significant ends and low pressure ammonia---the import of water vapor is connected with another outlet of a superheater, and the outlet of the high pressure ammonia of secondary high temperature superheater---water vapor connects with the admission end of steam turbine; In extended surface tube beam evaporation device and economizer, identical multi-functional compound working medium is housed.
3, a kind of system that utilizes coke-oven gas, tar, flue gas combined generating and produce composite chemical fertilizer according to claim 1 and 2, it is characterized in that: described multi-functional compound working medium is made up of ammonia, water and tertiary sodium phosphate, earlier with ammonia and water with ammonia: water=25～28: 100 weight ratio is mixed with ammoniacal liquor, and then again with tertiary sodium phosphate: ammoniacal liquor=weight ratio of 10: 100 is mixed with the multi-functional compound working medium of PH10～11.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006101021617A CN100436379C (en) | 2006-11-13 | 2006-11-13 | System for united electricity generation using coke oven gas, tar oil, flume and producing composite fertilizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006101021617A CN100436379C (en) | 2006-11-13 | 2006-11-13 | System for united electricity generation using coke oven gas, tar oil, flume and producing composite fertilizer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1962558A true CN1962558A (en) | 2007-05-16 |
| CN100436379C CN100436379C (en) | 2008-11-26 |
Family
ID=38081809
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006101021617A Expired - Fee Related CN100436379C (en) | 2006-11-13 | 2006-11-13 | System for united electricity generation using coke oven gas, tar oil, flume and producing composite fertilizer |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102191957A (en) * | 2011-05-03 | 2011-09-21 | 金能科技有限责任公司 | Combined cycle and combined heat and power (CHP) equipment and process |
| CN103111172A (en) * | 2013-01-15 | 2013-05-22 | 大连海事大学 | System and method for waste heat recovery and tail gas treatment of marine main engine |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1487174A (en) * | 2003-08-25 | 2004-04-07 | 刘金郎 | Combined circular generator with gas and hydrocarbon oil gas turbine and steam turbine |
| CN1269735C (en) * | 2003-10-20 | 2006-08-16 | 邰学林 | Combined gasification process of producing synthetic ammonia |
| CN100338424C (en) * | 2004-09-30 | 2007-09-19 | 中信重型机械公司 | Generating set system of simple low temperature waste heat from large size cement manufacture line in dry method, and technical process |
-
2006
- 2006-11-13 CN CNB2006101021617A patent/CN100436379C/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102191957A (en) * | 2011-05-03 | 2011-09-21 | 金能科技有限责任公司 | Combined cycle and combined heat and power (CHP) equipment and process |
| CN102191957B (en) * | 2011-05-03 | 2014-05-21 | 金能科技股份有限公司 | Combined cycle and combined heat and power (CHP) equipment and process |
| CN103111172A (en) * | 2013-01-15 | 2013-05-22 | 大连海事大学 | System and method for waste heat recovery and tail gas treatment of marine main engine |
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| Publication number | Publication date |
|---|---|
| CN100436379C (en) | 2008-11-26 |
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Granted publication date: 20081126 Termination date: 20151113 |