CN204550484U - A kind of chilling process vapourizing furnace with high-temperature hot retrieving arrangement - Google Patents
A kind of chilling process vapourizing furnace with high-temperature hot retrieving arrangement Download PDFInfo
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- CN204550484U CN204550484U CN201520124087.3U CN201520124087U CN204550484U CN 204550484 U CN204550484 U CN 204550484U CN 201520124087 U CN201520124087 U CN 201520124087U CN 204550484 U CN204550484 U CN 204550484U
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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]
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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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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Abstract
The utility model discloses a kind of chilling process vapourizing furnace with high-temperature hot retrieving arrangement, comprise the gasification/burn room on top, middle part there is the radiation waste pot of high temperature heat recovery function and the scrubbing-cooling chamber of bottom.The body of heater top of gasification/burn room or certain plane of body of heater periphery or multiple plane arrange one or more nozzle.Radiation waste pot is made up of the flange be connected with gasification/burn room, interface water-cooled coil pipe, single passage water wall, the water-cooled coil pipe etc. that is connected with scrubbing-cooling chamber.Scrubbing-cooling chamber primarily of Quench water ring and downtake composition, and is provided with syngas outlet above scrubbing-cooling chamber side.The utility model can improve the adaptability of coal, the high-order sensible heat of efficient recovery gasification product, is applicable to process unit and the integrated gasification combined cycle for power generation system of preparing synthetic gas.Relative to traditional pot destroying process vapourizing furnace, its structure is comparatively simple, makes with easy to maintenance, has higher promotion and application and is worth.
Description
Technical field
The utility model belongs to gasification field, relates to a kind of airflow bed gasification furnace with radiation waste pot and scrubbing-cooling chamber, is a kind of can to reclaim the sensible heat of high-temperature synthesis gas after gasification and for the preparation of synthetic gas (CO+H
2) gasification installation.
Background technology
The energy and important source material based on coal, have important strategic position in national economy and social development.Chemical Industry is the important industry of Coal Clean Efficient Conversion, and through the development of nearly decades, China's Coal Chemical Industry general technical levels is very fast, but still there is the problems such as energy consumption is high, pollution is comparatively serious, resource utilization is low.Energy-efficient Coal Gasification Technology is the core technology of coal chemical industry development and leading technology.Exploitation is suitable for the energy-efficient Coal Gasification Technology of methyl alcohol, ethylene glycol and hydrocarbon synthesis (F-T synthesis); to the sustainable efficiency utilization of promotion resource, realize pollutent near zero release, protection of the environment; ensure national energy security, promote that the sustainable scientific development of national economy has great strategic importance.
In High Temperature High Pressure downstream bed coal-gasification process, transmittance process plays an important role, technique means and the Exposure degree mode of different strengthening transfer process create multi-form airflow bed gasification furnace, mainly containing with coal water slurry is Coal-water slurry gasification with opposed multi-burners, GE (Texaco), the Global E-gas technology of raw material, take dried coal powder as Shell, GSP technology of raw material.Based on the demand of gasification following process variant production, and reclaim the difference of coal gas of high temperature sensible heat process program, gasifying process mainly comprises: chilling process, pot destroying process and useless pot Quench combined process flow.The cold gas efficiency about 72 ~ 76% of air flow bed coal water slurry gasification technology, in coal, the calorific value of more than 20% exists with the sensible heat of coal gas.The cold gas efficiency about 83% of Dry Feeding Entrain Bed Coal Gasification Technology, in coal, the calorific value of about 14% exists with the sensible heat of coal gas.Fully, effectively utilize the sensible heat of coal gas of high temperature, for entrained flow gasification, particularly coal water slurry gasification is energy-saving and cost-reducing significant.
The technique of chilling process, equipment and operation are all comparatively simple, are mainly used in Coal Chemical Engineering Project, have reached its maturity and perfect.But from Energy harvesting angle, mainly there is the shortcomings such as thermo-efficiency is low, the wasting of resources is large, energy utilization is unreasonable in chilling-type vapourizing furnace.Compared with pot destroying process, heating gas decrease in efficiency 5 ~ 8%.Pot destroying process to be given up the heat recuperation of the coal gas of high temperature, slag etc. of about 1400 DEG C that pot will produce in gasification by radiation waste pot and convection current, the recyclable energy being equivalent to feed coal net calorific value 15 ~ 18%, by-product saturation steam, generate electricity for steam turbine in IGCC, realize heat recovery and utilization, make heating gas efficiency reach 90 ~ 95%.But because the equipment complexity of pot destroying process, troublesome poeration, investment are very large, so that cannot promote on a large scale.Therefore, develop a kind of gasification installation simultaneously realizing high temperature Exposure degree and Quench, make two kinds of modes organically combine the advantage can taking into account both, finally reach stable operation and reduce the objects such as facility investment.
Utility model content
In view of the above problems, the purpose of this utility model is day by day to improve and widely used multiple-nozzle contraposition type coal water slurry gasification stove based in modern production firm, there is provided a kind of with radiation waste pot and Quench combined process flow to reclaim the vapourizing furnace of coal gas of high temperature sensible heat, to meet methyl alcohol, ethylene glycol and hydrocarbon synthesis (F-T synthesis) technical field, the efficient energy-saving coal gasification technical need of IGCC power field.
Mentality of designing of the present utility model is as follows: with the vapourizing furnace of high-temperature hot retrieving arrangement, body of heater top or certain plane of body of heater periphery or multiple plane arrange the gasification/burn room with this nozzle one or more, adopt radiation waste pot to reclaim coal gas of high temperature sensible heat, there is the raw gas wash cooling device adopting Water spray cooling.The crude synthesis gas temperature going out gasification/combustion chamber is 1100 ~ 1500 DEG C, is cooled to about 600 ~ 950 DEG C through radiation waste pot, then is cooled to about 150 ~ 250 DEG C through scrubbing-cooling chamber.The steam-energy relying on gas heat to produce meets the requirement of rear operation Partial Transformation.Radiation waste pot produces high pressure steam, and be used as power steam or driving turbine, can reduce steam coal consumption, thus the energy consumption of obvious reduction system;
The metal shell of vapourizing furnace can bear High Temperature High Pressure, and the gasification/burn chamber liner refractory brick on top, can improve service temperature, for radiation waste pot provides heat to promote steam quality.Therefore, this vapourizing furnace can process the high coal of ash fusion point;
The gasification slag notch of the gasification/burn room on top adopts refractory liner reducing design, and gasification slag notch and radiation waste pot entrance adopt Flange joint, the split type manufacture of equipment of being convenient to, installation and transport.Bottom gasification slag notch, metal profile is set, for supporting vapourizing furnace cinder notch refractory brick.Below this back up pad, adopt horizontal plate tubular type water wall structure to be also coated with silicon carbide in the outside of inner ring, can reduce on the one hand vaporizer high-temperature synthesis gas and lime-ash on the impact of equipment, slag notch brick back up pad temperature can be maintained on the other hand, avoid overtemperature;
Radiation waste pot entrance is para-curve or tapered flaring structure, adopts water wall structure and is coated with silicon carbide protection water wall coil pipe.This is designed with and is beneficial to slag and falls into radiation waste pot, and reduces inlet jet recirculating zone to the impact of the particle depositions such as slag at radiation waste pot entrance water wall wall;
The water wall of radiation waste pot adopts single cylinder structure design, and be provided with fin type water wall in water-cooled wall barrel, this fin type water wall is arranged at radiation waste pot direct tube section;
The connection of radiation waste pot slag notch and wash cooling chamber inlet is the coil wall structure of tapered reducing, the metal baffle of the water wall inner ring welding conical surface, one circle water ring being set at upper cone mouth circumferential direction, putting only radiation waste pot slag notch blocking by regulating injection flow rate;
Scrubbing-cooling chamber is arranged at radiation waste pot bottom, and is provided with downtake.Gas and enter scrubbing-cooling chamber through downtake through the cooled lime-ash of radiation waste pot, complete the rough purification of gas, lime-ash by entering the water-bath bottom scrubbing-cooling chamber, and is discharged through lock hopper.Synthetic gas enters subsequent processing via the syngas outlet be arranged on above scrubbing-cooling chamber side.
Concrete technical scheme is as follows:
With a chilling process vapourizing furnace for high-temperature hot retrieving arrangement, comprise metal shell 1, be placed in the gasification/burn room 11 of metal shell 1 inside and the radiation waste pot 2 be in successively below described metal shell 1 and scrubbing-cooling chamber 3;
Have the slag notch 14 that gasifies between described gasification/burn room 11 and radiation waste pot 2, connect radiation waste pot interface 21 below described gasification slag notch 14, the below of described radiation waste pot interface 21 connects water wall 24; It is inner that described radiation waste pot interface 21 and water wall 24 are all placed in described radiation waste pot 2;
There is between described radiation waste pot 2 and scrubbing-cooling chamber 3 radiation waste pot slag notch 27; The radiation waste pot 2 in the middle part of vapourizing furnace is utilized to reclaim the sensible heat of the high-temperature synthesis gas that upper air bed coal slurry gasifier produces;
The below of described radiation waste pot slag notch 27 has the downtake 31 be placed in described scrubbing-cooling chamber 3, has been horizontally disposed with Quench water ring 35 between described radiation waste pot slag notch 27 and described downtake 31.
Described gasification/burn room 11 is air flow bed form, and its liner is firebrick structure or water wall structure.
Described metal shell 1 can bear not higher than the high pressure of 10.0MPa, and the internal diameter of described gasification/burn room 11 is 2.5 ~ 6.0m; The internal diameter of described radiation waste pot 2 is 3.0 ~ 8.0m, and aspect ratio is 3 ~ 10, adopts single passage water wall structure.
Described gasification slag notch 14 is Flange joint with the connection of described radiation waste pot interface 21, and be provided with the cinder notch back up pad 15 of metal material bottom described gasification slag notch 14, described cinder notch back up pad 15 is for supporting the refractory lining of vapourizing furnace slag notch 14.
Described radiation waste pot interface 21 is the water wall structure of parabolic type or tapered downward enlarging and scribbles silicon carbide, and the water wall of downward enlarging adopts coil form, is positioned at immediately below described cinder notch back up pad 15.
Described radiation waste pot slag notch 27 is the tapered water wall structures shunk gradually to described scrubbing-cooling chamber 3 Way in, and described tapered water wall adopts coil form.
The liner of described radiation waste pot slag notch 27 has conical surface metal baffle, and the upper cone mouth circumferential direction of described conical surface metal baffle is provided with a circle water ring 26, described water ring 26 offers some spout holes 28 for rinsing the lime-ash being deposited on bottom.
Described metal shell 1 outside offers opposed burner mouth 12.
The top of described water wall 24 has water wall entrance 22 and water wall outlet 23, and described water wall entrance 22 and water wall outlet 23 extend to the outside of described radiation waste pot 2.
Described scrubbing-cooling chamber 3 outside has chilled water entrance 32, syngas outlet 33 and Heisui River outlet 34, and described Heisui River outlet 34 is positioned at the below of described chilled water entrance 32 and syngas outlet 33.
Described chilling process vapourizing furnace, to can be used for carbon containing class materials such as coal water slurry, for the coal chemical engineering equipment of synthetic gas prepared by raw material, can be applicable to methanol, ethylene glycol, hydrocarbon synthesis and combined cycle generation field.
The utility model has following technological merit:
(1) the synthetic gas preparation technology that to be applicable to carbonaceous fuels such as coal water slurry be raw material, be applied to methanol, ethylene glycol, hydrocarbon synthesis and combined cycle generation field, byproduct steam can be obtained simultaneously, meet the requirement of conversion, Coal Chemical Industry is particularly synthesized to wet goods technique have suitability for ammonia from coal, F-T;
(2) size of this vapourizing furnace is less than normal compared with conventional radiation pot entirety of giving up, and reduces facility investment, adopts that single passage water wall structure is convenient to be manufactured and install, and is applicable to IGCC polygenerations systeme;
(3) coal adaptability is wide, can require that high high-ash-fusion coal carries out heat efficient recovery to service temperature, improves the utilising efficiency of the energy;
(4) gasification slag notch and radiation waste pot entrance structure can ensure passing through smoothly of high-temperature ash, arrange water ring simultaneously radiation waste pot can be avoided to export dust stratification at radiation waste pot slag notch;
(5) synthetic gas obviously reduces entering its bottom wash cooling room temperature after radiation waste pot, and the cooling water inflow more traditional Quench type vapourizing furnace now entering scrubbing-cooling chamber will significantly reduce, and can save quantity of circulating water, reduces running cost.
Accompanying drawing explanation
Fig. 1 is the chilling process vapourizing furnace agent structure schematic diagram of the band high-temperature hot retrieving arrangement of embodiment 1;
Fig. 2 is the structural representation of radiation waste pot slag notch water ring.
Nomenclature
1 metal shell; 2 radiation waste pots; 3 scrubbing-cooling chambers; 11 gasification/burn rooms;
12 burner mouths; 13 water wall or lining of fire brick; 14 gasification slag notches;
15 cinder notch back up pads; 16 flanges; 21 radiation waste pot interfaces; 22 water wall entrances;
23 water wall outlets; 24 water wall; 25 water ring entrances; 26 water rings;
27 radiation waste pot slag notches; 28 spout holes; 31 downtakes; 32 chilled water entrances;
33 syngas outlet; 34 Heisui River outlets; 35 Quench water rings; 36 vapourizing furnace slag-drip openings.
Embodiment
Embodiment 1
Fig. 1 is the structural representation of the chilling process vapourizing furnace of band high-temperature hot retrieving arrangement, Fig. 2 is the structural representation of radiation waste pot slag notch water ring, and the scrubbing-cooling chamber 3 primarily of the gasification/burn room 11 on top, the radiation waste pot 2 and bottom with high temperature heat recovery function at middle part is formed.It is inner that gasification/burn room 11 is placed in metal shell 1; Have the slag notch 14 that gasifies between gasification/burn room 11 and radiation waste pot 2, connect radiation waste pot interface 21 below gasification slag notch 14, the below of radiation waste pot interface 21 connects water wall 24; It is inner that radiation waste pot interface 21 and water wall 24 are all placed in radiation waste pot 2; There is between radiation waste pot 2 and scrubbing-cooling chamber 3 radiation waste pot slag notch 27; The below of radiation waste pot slag notch 27 has the downtake 31 be placed in scrubbing-cooling chamber 3, has been horizontally disposed with Quench water ring 35 between radiation waste pot slag notch 27 and downtake 31.Gasification/burn room 11 is air flow bed form, and its liner is water wall or lining of fire brick 13.Metal shell 1 ability is not more than the high pressure of 10.0MPa, and the internal diameter of gasification/burn room 11 is 2.5 ~ 6.0m; The internal diameter of radiation waste pot 2 is 3.0 ~ 8.0m, aspect ratio 3 ~ 10, adopts single passage water wall structure.Gasification slag notch 14 is that flange 16 connects with the connection of radiation waste pot interface 21, and be provided with the cinder notch back up pad 15 of metal material bottom gasification slag notch 14, cinder notch back up pad 15 is for supporting the refractory lining of vapourizing furnace slag notch 14.Radiation waste pot interface 21 is the water wall structure of parabolic type or tapered downward enlarging and scribbles silicon carbide, and the water wall of downward enlarging adopts coil form, is positioned at immediately below cinder notch back up pad 15.Radiation waste pot slag notch 27 is the tapered water wall structures shunk gradually towards scrubbing-cooling chamber 3 Way in, and tapered water wall adopts coil form.The liner of radiation waste pot slag notch 27 has conical surface metal baffle, and the upper cone mouth circumferential direction of conical surface metal baffle is provided with a circle water ring 26, water ring 26 offers some spout holes 28 for rinsing the lime-ash being deposited on bottom.Metal shell 1 outside offers opposed burner mouth 12.The top of water wall 24 has water wall entrance 22 and water wall outlet 23, and water wall entrance 22 and water wall outlet 23 extend to the outside of radiation waste pot 2.Scrubbing-cooling chamber 3 outside has chilled water entrance 32, syngas outlet 33 and Heisui River outlet 34, and Heisui River outlet 34 is positioned at the below of chilled water entrance 32 and syngas outlet 33.
High pressure water reclaims the high-temperature synthesis gas of gasification/burn room generation and the heat of lime-ash by water wall entrance 22 through single pass water wall entrance 24, and the high-quality steam produced can be used for power steam.Lime-ash and synthetic gas, before entering scrubbing-cooling chamber 3, may be deposited on the lime-ash of radiation waste pot slag notch 27, make it the downtake 31 entering scrubbing-cooling chamber 3 swimmingly via water ring 26 removing arranged in radiation waste pot 2.In downtake 31, complete further Quench, high-temperature ash particle falls into the vapourizing furnace slag-drip opening 36 bottom scrubbing-cooling chamber 3, and synthetic gas goes out vapourizing furnace through syngas outlet 33 after washing.
Certain single stove day process coal about 1500 tons of chilling process coal slurry gasifiers with high-temperature hot retrieving arrangement, oxygen and coal slurry enter vapourizing furnace through process burner, partial oxidation reaction is carried out in the interior gasification/burn being lined with refractory brick, vapor pressure 6.5MPa, gasification temperature about 1300 DEG C, effective gas (CO+H
2) output is about 100000Nm
3/ h.Gasification/burn room metal casing internal diameter 3.4m, radiation waste pot metal shell 4.4m, radiation waste pot height 25.0m, water wall diameter 3.0m, fin type water wall is along the circumferential direction evenly arranged.The high-temperature water temperature entering water wall is 319 DEG C, pressure 11.6MPa, and the vapor pressure 11.1MPa produced, quantity of steam is about 81t/h.
About 1300 DEG C of high-temperature synthesis gas that gasification/burn room produces and lime-ash enter radiation waste pot, and cool laggard scrubbing-cooling chamber synthetic gas temperature about 920 DEG C through radiation waste pot, synthetic gas goes out the temperature about 237 DEG C of scrubbing-cooling chamber, enters the scrubbing-cooling chamber Quench water yield and is about 227m
3/ h.Synthetic gas enters conversion section after washing, and now synthetic gas temperature about 226 DEG C, the battery limit (BL) that goes out to gasify enters water-gas ratio about 0.8 in the crude synthesis gas of conversion section, meets the processing requirement of CO Partial Transformation.
Overall gasification performance of the present utility model is as follows:
Gasification reaction temperature: 1300 DEG C;
Radiation waste pot outlet syngas temperatures: 920 DEG C;
Enter the front synthetic gas temperature of conversion: 226 DEG C;
Byproduct steam: 81t/h;
Consume than oxygen: 374Nm
3o
2/ 1000Nm
3(CO+H
2);
Than coal consumption: 573kg coal (butt)/1000Nm
3(CO+H
2);
Effective gas composition (CO+H
2): 82.3% (butt).
Although the foregoing describe embodiment of the present utility model, it will be understood by those of skill in the art that these only illustrate, protection domain of the present utility model is defined by the appended claims.Those skilled in the art, under the prerequisite not deviating from principle of the present utility model and essence, can make various changes or modifications to these embodiments, but these change and amendment all falls into protection domain of the present utility model.
Claims (10)
1. the chilling process vapourizing furnace with high-temperature hot retrieving arrangement, it is characterized in that, described chilling process vapourizing furnace comprises metal shell (1), is placed in the inner gasification/burn room (11) of metal shell (1) and is in radiation waste pot (2) and the scrubbing-cooling chamber (3) of described metal shell (1) below successively;
Between described gasification/burn room (11) and radiation waste pot (2), there is gasification slag notch (14), described gasification slag notch (14) below connects radiation waste pot interface (21), and the below of described radiation waste pot interface (21) connects water wall (24); Described radiation waste pot interface (21) and water wall (24) are all placed in described radiation waste pot (2) inside;
Between described radiation waste pot (2) and scrubbing-cooling chamber (3), there is radiation waste pot slag notch (27);
The below of described radiation waste pot slag notch (27) has the downtake (31) be placed in described scrubbing-cooling chamber (3), has been horizontally disposed with Quench water ring (35) between described radiation waste pot slag notch (27) and described downtake (31).
2. chilling process vapourizing furnace according to claim 1, is characterized in that, described gasification/burn room (11) is air flow bed form, and its liner is firebrick structure or water wall structure.
3. chilling process vapourizing furnace according to claim 1, is characterized in that, described metal shell (1) can bear not higher than the high pressure of 10.0MPa, and the internal diameter of described gasification/burn room (11) is 2.5 ~ 6.0m; The internal diameter of described radiation waste pot (2) is 3.0 ~ 8.0m, aspect ratio 3 ~ 10, adopts single passage water wall structure.
4. chilling process vapourizing furnace according to claim 1, it is characterized in that, described gasification slag notch (14) is Flange joint with the connection of described radiation waste pot interface (21), described gasification slag notch (14) bottom is provided with the cinder notch back up pad (15) of metal material, and described cinder notch back up pad (15) is for supporting the refractory lining of vapourizing furnace slag notch (14).
5. chilling process vapourizing furnace according to claim 1, it is characterized in that, described radiation waste pot interface (21) is the water wall structure of parabolic type or tapered downward enlarging and scribbles silicon carbide, the water wall of downward enlarging adopts coil form, is positioned at immediately below described cinder notch back up pad (15).
6. according to the arbitrary described chilling process vapourizing furnace of claim 1 to 5, it is characterized in that, described radiation waste pot slag notch (27) is the tapered water wall structure shunk gradually to described scrubbing-cooling chamber (3) Way in, and described tapered water wall adopts coil form.
7. chilling process vapourizing furnace according to claim 6, it is characterized in that, the liner of described radiation waste pot slag notch (27) has conical surface metal baffle, the upper cone mouth circumferential direction of described conical surface metal baffle is provided with a circle water ring (26), described water ring (26) offers some spout holes (28) for rinsing the lime-ash being deposited on bottom.
8. chilling process vapourizing furnace according to claim 1, is characterized in that, described metal shell (1) outside offers one or more burner mouth (12).
9. chilling process vapourizing furnace according to claim 1, it is characterized in that, the top of described water wall (24) has water wall entrance (22) and water wall outlet (23), and described water wall entrance (22) and water wall outlet (23) extend to the outside of described radiation waste pot (2).
10. chilling process vapourizing furnace according to claim 1, it is characterized in that, described scrubbing-cooling chamber (3) outside has chilled water entrance (32), syngas outlet (33) and Heisui River outlet (34), and described Heisui River outlet (34) is positioned at the below of described chilled water entrance (32) and syngas outlet (33).
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104629807A (en) * | 2015-03-03 | 2015-05-20 | 华东理工大学 | Chilling process gasifier with high-temperature heat recovery unit |
| CN105602629A (en) * | 2016-03-01 | 2016-05-25 | 上海锅炉厂有限公司 | Downlink high-temperature gasified product chilling device |
| CN106403000A (en) * | 2016-11-28 | 2017-02-15 | 郑州大学 | Rural small multifunctional biomass-energy heat-gas coproduction heating device |
| CN107033967A (en) * | 2016-02-04 | 2017-08-11 | 清华大学煤燃烧工程研究中心 | Coal gasification apparatus with heat recovery function |
| CN107033965A (en) * | 2016-02-04 | 2017-08-11 | 清华大学煤燃烧工程研究中心 | Gasification furnace with heat recovery system |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN104629807A (en) * | 2015-03-03 | 2015-05-20 | 华东理工大学 | Chilling process gasifier with high-temperature heat recovery unit |
| CN107033967A (en) * | 2016-02-04 | 2017-08-11 | 清华大学煤燃烧工程研究中心 | Coal gasification apparatus with heat recovery function |
| CN107033965A (en) * | 2016-02-04 | 2017-08-11 | 清华大学煤燃烧工程研究中心 | Gasification furnace with heat recovery system |
| CN105602629A (en) * | 2016-03-01 | 2016-05-25 | 上海锅炉厂有限公司 | Downlink high-temperature gasified product chilling device |
| CN105602629B (en) * | 2016-03-01 | 2018-08-24 | 上海锅炉厂有限公司 | A kind of downstriker high-temperature gasification product chilling device |
| CN106403000A (en) * | 2016-11-28 | 2017-02-15 | 郑州大学 | Rural small multifunctional biomass-energy heat-gas coproduction heating device |
| CN106403000B (en) * | 2016-11-28 | 2021-09-10 | 郑州大学 | Rural small-size multi-functional biomass energy steam coproduction heating system |
| CN108488785A (en) * | 2018-04-28 | 2018-09-04 | 东方电气集团东方锅炉股份有限公司 | A kind of fractional combustion supercharged oxygen-enriched boiler system |
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