CN109251753A - A kind of the thermoelectricity cold air co-feeding system and technique of renewable energy cooperative compensating - Google Patents
A kind of the thermoelectricity cold air co-feeding system and technique of renewable energy cooperative compensating Download PDFInfo
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- CN109251753A CN109251753A CN201810513004.8A CN201810513004A CN109251753A CN 109251753 A CN109251753 A CN 109251753A CN 201810513004 A CN201810513004 A CN 201810513004A CN 109251753 A CN109251753 A CN 109251753A
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/005—After-treatment of coke, e.g. calcination desulfurization
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K3/00—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
- C10K3/02—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by catalytic treatment
- C10K3/023—Reducing the tar content
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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
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/133—Renewable energy sources, e.g. sunlight
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The present invention relates to a kind of thermoelectricity cold air co-feeding system of renewable energy cooperative compensating and techniques.Renewable energy in the present invention mainly includes biomass energy, solar energy and house refuse energy.The solar energy, biomass energy and house refuse can be after conversions, through heat exchange and hold over system, and centralized heat energy supply can be used for warming oneself, and can also generate cold air cooling supply by refrigeration machine；House refuse generates medium calorific value gas, combustion-supporting combustion gas of a part as waste of low heating value coke melt-combustion after passing through low temperature pyrogenation respectively after the biomass and sorting；The pyrolysis of the house refuse completely cuts off air thermal dissociation using the rotary pyrolysis oven of outer heat, no dioxin generation, rubbish coke pyrolysis gas combustion-supporting lower melt-combustion temperature up to 1300 DEG C or more, thoroughly decompose dioxin；The present invention utilizes the characteristic of three kinds of renewable energy, and cooperative compensating constructs the thermoelectricity cold air co-feeding system of a set of pollution-free high-efficient rate.
Description
Technical field
The present invention relates to a kind of thermoelectricity cold air co-feeding system of renewable energy cooperative compensating and technique, belong to biomass,
Solar energy and house refuse energy cooperative compensating application field
Background technique
Currently, the basic annual acceleration of global energy consumption is incremented by, fossil energy resource is reduced year by year, and energy shortages highlights
The huge market potential of Renewable Energy Resources.After it experienced multiple world oil crisis, in the world to renewable energy
The understanding and development of the road utilized extensively in source again.China is a large agricultural country, and about 50% inhabitants live is in rural area
Area, one side biomass resource is extremely abundant, and agricultural straw resource total amount is equivalent to more than 3.17 hundred million tons up to more than 7.4 hundred million tons
Standard coal；Another aspect rural energy is generally short, and with can also be in, dependence is low-grade to utilize biomass energy rank for life in the countryside
Section, energy availability and demand contradiction is very prominent, have every year more than 200,000,000 tons of biomass straw discarded or it is waste burn, cause serious sky
Gas pollution and haze, greatly affected society, economy, environment, ecology and people's lives, become the one of governments at all levels' concern
A serious social concern.
For solar energy as the inexhaustible energy and its spatter property, Solar use is that the alleviation energy is short
It lacks, reduces the effective means of environmental pollution.
As process of modernization constantly accelerates, house refuse waste discharge capacity is growing day by day.Traditional garbage disposal
Method causes serious soil and atmosphere pollution, it is difficult to adapt to the demand of sustainable development.Domestic rubbish disposal of the present invention uses rubbish
Rubbish is pyrolyzed molten processing system, and the technology is compared to current universal trash processing way, such as sanitary landfills, biochemical compost and directly
It burns, pyrolysis fusion technology can reduce the pollution of dioxin and heavy metal, and current American, West Europe and Japan and other countries are generally transported
Domestic waste is handled with pyrolysis fusion technology.Fusion technology requires the Lower heat value of rubbish to reach 6000~7000KJ/Kg
More than, and only 4000KJ/Kg or so, the MSW heating value in rural area are lower for the rubbish Lower heat value in the more developed city in China.Cause
This present invention combines the pyrolysis of biomass with rubbish fusion technology, and pyrolysis gas of biomass melts assisted gas as rubbish,
Solve the problems, such as that China's rubbish is low using the calorific value encountered during pyrolysis fusion technology.
Summary of the invention
The purpose of the present invention is to propose to a kind of thermoelectricity cold air co-feeding system of renewable energy cooperative compensating and techniques, will give birth to
Substance energy, solar energy and house refuse can combine cooperative compensating between the energy, both solve China's house refuse using heat
The low problem of the calorific value encountered during solution fusion technology, also achieves the resource utilization of house refuse, alleviates fossil fuel
Consumption, mitigate the pressure of environmental pollution, improve living environment.
To achieve the goals above, the present invention adopts the following technical scheme:
A kind of the thermoelectricity cold air co-feeding system and technique of renewable energy cooperative compensating, the system comprises house refuse machines
Tool separation unit, the rotary pyrolysis oven of outer heat, flue gas Quench unit, rubbish coke sieve unit, rubbish coke decanter type melt-combustion
Bed concentrates heat exchange unit, refrigeration unit, the damaged forming unit of biomass sorting, biomass bubbling bed pyrolysis oven, tar high temperature to urge
Change cracking purification device, medium calorific value gas pipe network, solar energy vacuum tube heat collection unit, conduction oil cycling element, phase transformation salt accumulation of heat
Unit, biology burnt fluid-bed combustion furnace, high-temperature heat pipe.
The thermoelectricity cold air co-feeding system process flow of renewable energy cooperative compensating is as follows:
(1) biomass sorts damaged forming unit by biomass and enters the pyrolysis of biomass bubbling bed pyrolysis oven, conversion
For biological burnt and blended tars gas；Biological coke burns in biological burnt fluid-bed combustion furnace, and a part of thermal energy passes through high-temperature heat pipe
Pyrolysis oven is passed to, a part heat, which enters, concentrates heat exchange unit；Plant ash is as urban afforestation inorganic fertilizer after burning；Blended tars
Gas cracks purification device generation medium calorific value gas by tar high-temperature catalytic and heat, medium calorific value gas enter medium calorific value gas pipe
Net, combustion-supporting combustion gas of a portion medium calorific value gas as rubbish coke decanter type melt-combustion bed, a part are used as civilian combustion
Gas or industrial combustion gas, this Some gases can also directly clean burning, be converted into heat source or cold source；The heat of generation converges to concentration and changes
Hot cell；
(2) house refuse first passes around house refuse mechanical sorting unit for the iron in rubbish, nonferrous metal, glass equal part
It elects, the rubbish after sorting enters back into the rotary pyrolysis oven pyrolysis of outer heat, is pyrolyzed the blended tars gas and biomass of generation
The tar gas that pyrolysis generates, which is mixed, generates medium calorific value gas and heat into tar high-temperature catalytic cracking purification device；Pyrolysis produces
Raw rubbish coke is sent to burning in rubbish coke decanter type melt-combustion bed through the screening of rubbish coke sieve unit and handles, molten slag
It can be used as building and roadbed material after cooling；The high-temperature flue gas of rubbish coke decanter type melt-combustion bed melt-combustion enters outer heat and returns
Heat source of the rotatable pyrolysis oven as domestic garbage pyrolysis is chilled to outside 200 DEG C or less by the flue gas of the outer rotary pyrolysis oven of heat
Row；
(3) thermal-arrest, conduction oil cycling element and phase transformation salt accumulation of heat list of the solar energy Jing Guo solar energy vacuum tube heat collection unit
The accumulation of heat of member, thermal energy are transported to concentration heat exchange unit, can be used for heating, and can also pass through refrigeration unit cooling supply.
The beneficial effects of the present invention are:
(1) biomass is by the medium calorific value gas generated after pyrolysis, and a part is as low heat value house refuse melt-combustion
Combustion-supporting combustion gas, solve the problems, such as that China's house refuse is low using the calorific value that encounters during pyrolysis fusion technology.
(2) biomass pyrolytic is high using the biomass bubbling bed pyrolysis oven heat transfer efficiency based on high-temperature heat pipe, gas production is big,
Using self-produced combustion gas as fluidizing agent, nitrogen content is few in combustion gas, and calorific value is high.
(3) hot rotary pyrolysis oven is wide to the adaptability of house refuse form outside, and treating capacity is big, and pyrolysis gas calorific value is high；And
Completely cut off air thermal dissociation, no dioxin generates.
(4) for rubbish coke in the combustion-supporting lower melt-combustion of pyrolysis gas, temperature thoroughly decomposes dioxin up to 1300 DEG C or more, heavy
It is metal-cured in slag.
(5) blended tars gas cracks purification device by tar high-temperature catalytic, and coke tar cracking is at combustion gas and releases heat,
Reach the purification of pyrolysis gas, no phenol wastewater generates.
Detailed description of the invention
Fig. 1 is the present invention a kind of the thermoelectricity cold air co-feeding system and process flow diagram of renewable energy cooperative compensating；
Fig. 2 is the flow diagram that the present invention is applied to resident's heating cooling supply；
Fig. 3 is the flow diagram that the present invention is applied to resident's power supply heating cooling supply；
Fig. 4 is the flow diagram that the present invention is applied to resident's heating cooling supply gas supply power supply.
Specific embodiment
The present invention is further described with embodiment with reference to the accompanying drawing.
Present system include: house refuse mechanical sorting unit 1, the rotary pyrolysis oven 2 of outer heat, flue gas Quench unit 3,
Rubbish coke sieve unit 4, rubbish coke decanter type melt-combustion bed 5 concentrate heat exchange unit 6, refrigeration unit 7, biomass sorting broken
Damage forming unit 8, biomass bubbling bed pyrolysis oven 9, tar high-temperature catalytic cracking purification device 10, medium calorific value gas pipe network 11,
The burnt fluid-bed combustion furnace of solar energy vacuum tube heat collection unit 12, conduction oil cycling element 13, phase transformation salt thermal storage unit 14, biology
15, high-temperature heat pipe 16.
Rotary 2 heat source of pyrolysis oven of outer heat is the high-temperature flue gas of rubbish coke decanter type melt-combustion bed 5, high-temperature flue gas
With house refuse indirect heat exchange.
1300 DEG C of ignition temperature or more of the rubbish coke decanter type melt-combustion bed 5, combustion-supporting combustion gas are fired from middle calorific value
Gas pipe network 11.
The biomass bubbling bed pyrolysis oven 9 is using high-temperature heat pipe as heat transfer element.
Tar high-temperature catalytic cracking purification device 10 divides for two sections, and 700 DEG C of upper section temperature, lower section temperature 1100
DEG C, tar cracks purification device 10 by tar high-temperature catalytic and generates combustion gas and heat.
The slag that the rubbish coke decanter type melt-combustion bed 5 generates can be used as building and roadbed material.
The lime-ash (plant ash) that the burnt fluid-bed combustion furnace 15 of biology generates can be used as urban afforestation inorganic fertilizer.
The thermoelectricity cold air co-feeding system process flow of renewable energy cooperative compensating is as follows:
(1) biomass sorts damaged forming unit 8 by biomass and enters the pyrolysis of biomass bubbling bed pyrolysis oven 9, turns
Turn to biological burnt and blended tars gas；Biological coke burns in biological burnt fluid-bed combustion furnace 15, and a part of thermal energy passes through high temperature
Heat pipe 16 passes to pyrolysis oven, and a part heat, which enters, concentrates heat exchange unit 6；Plant ash is as urban afforestation inorganic fertilizer after burning；
Blended tars gas cracks purification device 10 by tar high-temperature catalytic and generates medium calorific value gas and heat, during medium calorific value gas enters
Calorific value fuel gas pipe network 11, combustion-supporting combustion gas of a portion medium calorific value gas as rubbish coke decanter type melt-combustion bed 5, one
It is allocated as domestic gas；The heat of generation, which converges to, concentrates heat exchange unit 6；
(2) house refuse first passes around house refuse mechanical sorting unit 1 for iron, nonferrous metal, the glass etc. in rubbish
It sorts out, the rubbish after sorting enters back into the rotary pyrolysis oven 2 of outer heat and is pyrolyzed, and is pyrolyzed the blended tars gas and biology of generation
The tar gas that matter pyrolysis generates, which is mixed, generates medium calorific value gas and heat into tar high-temperature catalytic cracking purification device 10；Heat
It solves the rubbish coke generated and is sent to burning processing in rubbish coke decanter type melt-combustion bed 5 through the screening of rubbish coke sieve unit 4, melt
It can be used as building and roadbed material after melting slag is cooling；The high-temperature flue gas of 5 melt-combustion of rubbish coke decanter type melt-combustion bed into
Enter heat source of the rotary pyrolysis oven 2 of outer heat as domestic garbage pyrolysis, is chilled to by the flue gas of the rotary pyrolysis oven 2 of outer heat
200 DEG C or less outlets；
(3) thermal-arrest, conduction oil cycling element 13 and phase transformation salt of the solar energy Jing Guo solar energy vacuum tube heat collection unit 12 store
The accumulation of heat of hot cell 14, thermal energy, which is transported to, concentrates heat exchange unit 6, can be used for heating, can also pass through 7 cooling supply of refrigeration unit.
This system can need to provide different products according to different users, such as:
(1) cold and hot supply, as shown in Figure 2:
For 100 family resident's warmings, 7.5 ton/days of biomass consumption, 0.75 ton of domestic rubbish disposal amount/
It, can produce the heat (cold) of 780KW/h, 0.9 ton/day of plant ash (urban afforestation inorganic fertilizer), 0.23 ton/day of slag
(building and roadbed material)；In addition solar energy can supply the heat (cold) of 195KW/h.
(2) thermoelectricity cold supply, as shown in Figure 3:
For 86 family resident's warmings, 7.5 ton/days of biomass consumption, 0.75 ton/day of domestic rubbish disposal amount,
The heat (cold) of 550KW/h, 3300Nm can be produced3The combustion gas in/day, 0.9 ton/day of plant ash (urban afforestation inorganic fertilizer),
0.23 ton/day of slag (building and roadbed material)；Wherein combustion gas is completely used for fuel cell power generation for resident's use, power generation rule
Mould 360KW；In addition solar energy can supply the heat (cold) of 195KW/h.
(2) thermoelectricity cold air is supplied, as shown in Figure 4:
For 86 family resident's warmings, 7.5 ton/days of biomass consumption, 0.75 ton/day of domestic rubbish disposal amount,
The heat (cold) of 550KW/h, 3300Nm can be produced3The combustion gas in/day, 0.9 ton/day of plant ash (urban afforestation inorganic fertilizer),
0.23 ton/day of slag (building and roadbed material)；Part of combustion gas 172Nm3/ day is used for resident, another part combustion gas
It is used for fuel cell power generation for resident, generate electricity scale 340KW；In addition solar energy can supply the heat (cold) of 195KW/h.
Claims (8)
1. the thermoelectricity cold air co-feeding system and technique of a kind of renewable energy cooperative compensating, which is characterized in that the system comprises
House refuse mechanical sorting unit, the rotary pyrolysis oven of outer heat, flue gas Quench unit, rubbish coke sieve unit, the sedimentation of rubbish coke
Formula melt-combustion bed, concentrate heat exchange unit, refrigeration unit, biomass sort damaged forming unit, biomass bubbling bed pyrolysis oven,
Tar high-temperature catalytic crack purification device, medium calorific value gas pipe network, solar energy vacuum tube heat collection unit, conduction oil cycling element,
Phase transformation salt thermal storage unit, biology burnt fluid-bed combustion furnace, high-temperature heat pipe.
2. the thermoelectricity cold air co-feeding system and technique of a kind of renewable energy cooperative compensating according to claim 1, feature
It is, the outer rotary pyrolysis oven heat source of heat is the high-temperature flue gas of rubbish coke decanter type melt-combustion bed, high-temperature flue gas and life
Rubbish indirect heat exchange living.
3. the thermoelectricity cold air co-feeding system and technique of a kind of renewable energy cooperative compensating according to claim 1, feature
It is, 1300 DEG C of ignition temperature or more of the rubbish coke decanter type melt-combustion bed, combustion-supporting combustion gas comes from medium calorific value gas pipe
Net.
4. the thermoelectricity cold air co-feeding system and technique of a kind of renewable energy cooperative compensating according to claim 1, feature
It is, the biomass bubbling bed pyrolysis oven is using high-temperature heat pipe as heat transfer element.
5. the thermoelectricity cold air co-feeding system and technique of a kind of renewable energy cooperative compensating according to claim 1, feature
It is, the tar high-temperature catalytic cracking purification device is divided into two sections, 700 DEG C of upper section temperature, 1100 DEG C of lower section temperature, burnt
Oil cracks purification device by tar high-temperature catalytic and generates combustion gas and heat.
6. the thermoelectricity cold air co-feeding system and technique of a kind of renewable energy cooperative compensating according to claim 1, feature
It is, the slag that the rubbish coke decanter type melt-combustion bed generates can be used as building and roadbed material.
7. the thermoelectricity cold air co-feeding system and technique of a kind of renewable energy cooperative compensating according to claim 1, feature
It is, the lime-ash (plant ash) that the burnt fluid-bed combustion furnace of biology generates can be used as urban afforestation inorganic fertilizer.
8. the thermoelectricity cold air co-feeding system and technique of a kind of renewable energy cooperative compensating according to claim 1, feature
It is, the thermoelectricity cold air co-feeding system process flow of renewable energy cooperative compensating is as follows:
(1) biomass sorts damaged forming unit by biomass and enters the pyrolysis of biomass bubbling bed pyrolysis oven, and conversion is made a living
Object coke and blended tars gas；Biological coke burns in biological burnt fluid-bed combustion furnace, and a part of thermal energy passes through high-temperature heat pipe and transmits
To pyrolysis oven, a part heat, which enters, concentrates heat exchange unit；Plant ash is as urban afforestation inorganic fertilizer after burning；Blended tars gas is logical
It crosses tar high-temperature catalytic cracking purification device generation medium calorific value gas and heat, medium calorific value gas enters medium calorific value gas pipe network,
Combustion-supporting combustion gas of the middle a part of medium calorific value gas as rubbish coke decanter type melt-combustion bed, a part are used as domestic gas or work
Industry combustion gas, this Some gases can also directly clean burning, be converted into heat source or cold source；It is single that the heat of generation converges to concentration heat exchange
Member；
(2) house refuse first passes around house refuse mechanical sorting unit and sub-elects iron, nonferrous metal, the glass etc. in rubbish
Come, the rubbish after sorting enters back into the rotary pyrolysis oven pyrolysis of outer heat, is pyrolyzed the blended tars gas and biomass pyrolytic of generation
The tar gas of generation, which is mixed, generates medium calorific value gas and heat into tar high-temperature catalytic cracking purification device；What pyrolysis generated
Rubbish coke is sent to burning in rubbish coke decanter type melt-combustion bed through the screening of rubbish coke sieve unit and handles, and molten slag is cooling
After can be used as building and roadbed material；It is rotary that the high-temperature flue gas of rubbish coke decanter type melt-combustion bed melt-combustion enters outer heat
Heat source of the pyrolysis oven as domestic garbage pyrolysis is chilled to 200 DEG C or less outlets by the flue gas of the outer rotary pyrolysis oven of heat；
(3) thermal-arrest of the solar energy Jing Guo solar energy vacuum tube heat collection unit, conduction oil cycling element and phase transformation salt thermal storage unit
Accumulation of heat, thermal energy are transported to concentration heat exchange unit, can be used for heating, and can also pass through refrigeration unit cooling supply.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114447374A (en) * | 2020-10-30 | 2022-05-06 | 上海汽车集团股份有限公司 | Hydrogen fuel cell cold start system, combined cooling heating and power system and combined cooling heating and power method |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2152561C1 (en) * | 1998-01-22 | 2000-07-10 | Институт проблем химической физики РАН | Condensed combustibles recovery method |
| CN1502420A (en) * | 2002-11-27 | 2004-06-09 | 中南大学 | Gasifying method and device for treating low thermal value fuel |
| CN101705114A (en) * | 2009-11-20 | 2010-05-12 | 昆明理工大学 | Method for preparing combustible gas by using rotary kiln to melt and gasify household garbage |
| CN102154044A (en) * | 2011-03-11 | 2011-08-17 | 周鼎力 | Method for preparing engine fuel gas by using biomass and/or organic waste |
| CN103277856A (en) * | 2013-05-28 | 2013-09-04 | 中国科学院广州能源研究所 | Solar seasonal cold and hot combined air conditioning system |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114447374A (en) * | 2020-10-30 | 2022-05-06 | 上海汽车集团股份有限公司 | Hydrogen fuel cell cold start system, combined cooling heating and power system and combined cooling heating and power method |
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Application publication date: 20190122 |