CN1730617A - Fuild bed composite circle coal gasification method and apparatus - Google Patents
Fuild bed composite circle coal gasification method and apparatus Download PDFInfo
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- CN1730617A CN1730617A CN 200510012754 CN200510012754A CN1730617A CN 1730617 A CN1730617 A CN 1730617A CN 200510012754 CN200510012754 CN 200510012754 CN 200510012754 A CN200510012754 A CN 200510012754A CN 1730617 A CN1730617 A CN 1730617A
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Abstract
The invention provides a fluid bed composite circle coal gasification method and apparatus, characterized in that, the coal material is preheated by a separator, then is fed into a gasification outer cylinder from an L valve in an upper ring chamber for gasification, the non-gasified coal coke enters a gasifying combustion inner cartridge, the separator, the L valve in the upper ring chamber and the gasifying outer cylinder for inner loop combustion and gasification from an L valve in a lower ring chamber, the gasified coal gas is loaded into a separator for output, the flue gas is imported into a fume separator for discharge, the separated flying coal or fly ash are gasified or discharged. The equipment can realize a heat output coefficient of 85-92%.
Description
Technical field
The present invention relates to a kind of method and apparatus of gasification, particularly a kind of method and apparatus that is used for fuild bed composite circle coal gasification.
Background technology
Gasification is one of gordian technique of Coal Chemical Industry.Coal Gasification Technology can be divided into air flow bed, fluidized-bed and fixed bed three major types.The main drawback of air flow bed is to need huge powder manufacturing apparatus, power consumption height for the system coal dust; In addition, nozzle life is short and refractory materials strict also be its defective place.In the static bed coal gasification process, remaining 5%～10% semicoke is difficult to gasification, itself and lime-ash together can only be discharged, and fixed bed gasification efficient can only have about 85%.In the fluidized-bed gasification process, material in round-robin process repeatedly, realize with vaporized chemical fully and Long contact time, the part that helps being difficult in the coal that is difficult to gasify and the coal gasification realizes gasification, can adapt to different rank coals and high grey low-quality coal gasification, no tar pollution deposits yields in the gasification, gasification operation temperature moderate (900 ℃～1100 ℃).Present inventor's the patent No. is in 03112381.3 the patent, has introduced a kind of method and apparatus of gasification, and it comprises the feed well heater that gasifying reactor, burning promote stove and have the coal preprocessing function; The patent No. is 01123960.3 to disclose powdered coal fluidized bed gasification method and vapourizing furnace, above patent all has coal combustion section and gasification section separated structures, the heat that its burning zone produces is brought gasification section into by high-temperature material fully, and this burning zone and gasification section separated structures increase equipment cooling, thus, this paper proposes a kind of burning of coal gasification and hockets, in coal combustion process reaches by the high-temperature material circulation, the heat passage of urceolus provides thermal source for coal gasification, realization comprises the high coal gasification method and the equipment of compact construction efficient of the compound cycle of internal recycle and outer circulation.
Summary of the invention
The object of the present invention is to provide a kind of burning of coal---gasification hockets, coal combustion process comprises the high coal gasification method and the equipment of efficient compound cycle, compact construction of internal recycle and outer circulation by the heat passage of high-temperature material circulation and inside and outside tube for coal gasification provides thermal source, realization.To solve coal in gasification, the problem that burning and gasification hocket, the problem of internal recycle and outer circulation compound cycle, the problem of the difficult gasification of semicoke in the coal gasification course.
The present invention realizes that inner cyclic process is to be made of burning inner core, separator, gasification urceolus and upper and lower ring casing L valve; The present invention realizes that the outer circulation process is to be made of gasification urceolus, coal gas separator, burning inner core, combustion exhaust separator, feed back control valve; The present invention realizes that the inside and outside coal gasification course that internal recycle gasification and outer circulation gasification combine constitutes the compound cycle gasification.
The present invention is a basic point with above-mentioned purpose and problem, and the fuild bed composite circle coal gasification method of proposition and the technical scheme of equipment are as follows:
Adopt a kind of method of gasification, to be coal charge entered in the ring casing L valve after by the separator preheating by ring-like coal inlet this method, the promotion gas that is promoted the gas inlet by last ring casing L valve pushes in the fluidized-bed gasification urceolus, the overheated steam that enters with the overheated steam inlet gasifies, wherein the coal tar of gasification does not enter down in the ring casing L valve, the promotion gas that is promoted the gas inlet by following ring casing L valve pushes in the fluidized-bed combustion lifting inner core, the pressurized air that enters with the compressed air inlet rises and carries out combustion gasification, wherein the coal tar of unburn gasification enters in the separator with burning gas and separates, coal tar after the separation enters in the ring casing L valve once more, and the promotion gas that promotes the gas inlet by last ring casing L valve pushes and carries out the internal recycle gasification in the fluidized-bed gasification urceolus once more;
In the fluidized-bed gasification urceolus, gasify the coal gas that produces by separating in the gas outlet tube input coal gas separator, coal gas after the separation is exported by gas exit, and 2. fly coal or flying dust after the separation are carried out by feed back control valve and ash-valve that outer circulation flies gasification or flying dust discharges outward;
In promoting inner core, fluidized-bed combustion gasifies the high-temp waste gas that produces by separating in the waste gas outlet pipe input combustion exhaust separator, high-temp waste gas after the separation is discharged outward by exhanst gas outlet, after the separation fly coal or flying dust 1. flies coal outer circulation gasification by feed back control valve and ash-valve or flying dust discharges outward;
The lime-ash that burning produces in fluidized-bed combustion lifting inner core is entered in the water sealed tank by the ash releasing tube of bottom.
Above-mentioned described coal charge is low volatile fine coal or anthracite fine coal.
The further method of above-mentioned described fuild bed composite circle coal gasification is that coal charge is entered in the separator by ring-like coal inlet, after being 570 ℃～600 ℃ by 40 ℃～80 ℃ preheatings, enter in the ring casing L valve, the promotion gas that is promoted the gas inlet by last ring casing L valve pushes in the fluidized-bed gasification urceolus, 200 ℃～250 ℃ the superheated vapour and the red-hot coal charge that are entered in the fluidized-bed gasification urceolus by the superheated vapour inlet carry out the combustion gasification reaction, wherein, the coal tar of unburn gasification reaction promotes promotion gas that the gas inlet enters by the following ring casing L valve of fluidized-bed gasification urceolus bottom and pushes fluidized-bed combustion and promote the pressurized air that enters with compressed air inlet and air distribution plate in the inner core and rise and carry out fluidized gasification once more, wherein, unburned coal tar enters in the separator with combustion gas flowing and separates, coal tar after the separation enters in the ring casing L valve once more, and the promotion gas that promotes the gas inlet by last ring casing L valve pushes and carries out the internal recycle gasification in the fluidized-bed gasification urceolus once more;
The coal gas that gasification reaction produces in the fluidized-bed gasification urceolus is sent into by gas outlet tube and is carried out gas solid separation in the coal gas separator, and the coal gas after the separation is exported by gas exit;
Promote the high-temp waste gas that the burning coal tar produces in the inner core in fluidized-bed combustion and heat coal charge with the coal charge countercurrent flow in separator, sent in the combustion exhaust separator by waste gas outlet pipe then and separate, the high-temp waste gas after the separation is discharged by exhanst gas outlet;
After in combustion exhaust separator and coal gas separator, separating fly coal or flying dust by feed back control valve and ash-valve 1., 2. ash-valve carry out outer circulation and fly to discharge outside gasification or the flying dust;
The lime-ash that burning produces in fluidized-bed combustion lifting inner core is entered in the water sealed tank by the ash releasing tube of bottom.
The present invention adopts a kind of equipment of realizing coal gasification method, this equipment comprises: ring-like coal inlet, separator, the inner core sleeve pipe, last ring casing L valve, last ring casing L valve promotes the gas inlet, the fluidized-bed gasification urceolus, fluidized-bed combustion promotes inner core, following ring casing L valve, following ring casing L valve promotes the gas inlet, air distribution plate, the compressed air inlet, ash releasing tube, water sealed tank, waste gas outlet pipe, exhanst gas outlet, the combustion exhaust separator, gas outlet tube, gas exit, coal gas separator, ash-valve 1., the feed back pipe, ash-valve 2., the feed back control valve, the superheated vapour inlet, its constitutional features is:
A fluidized-bed combustion promotes inner core, is arranged with the fluidized-bed gasification urceolus outside it, and the top is connected with inner core sleeve pipe and separator, and the bottom is connected with air distribution plate and compressed air inlet and ash releasing tube and water sealed tank;
A fluidized-bed gasification urceolus is arranged with fluidized-bed combustion and promotes inner core in it, outer top is connected with ring casing L valve, goes up ring casing L valve promotion gas inlet, gas outlet tube; Outer bottom is connected with down ring casing L valve, ring casing L valve promotes gas inlet, superheated vapour inlet and feed back pipe down; The top is connected with separator and ring-like coal inlet; The bottom is connected with air distribution plate and compressed air inlet and ash releasing tube and water sealed tank;
A separator, its lower end are connected with fluidized-bed gasification urceolus and inner core sleeve pipe and fluidized-bed combustion and promote inner core, and the upper end is provided with ring-like coal inlet, and the side is communicated with the combustion exhaust separator by waste gas outlet pipe;
A coal gas separator, the one upper lateral part is communicated with the fluidized-bed gasification urceolus by gas outlet tube, and the upper end is provided with gas exit, and the bottom is communicated with feed back pipe and feed back control valve, and 2. the bottom is provided with ash-valve;
A combustion exhaust separator, the one upper lateral part is connected with separator by waste gas outlet pipe, and the upper end is provided with exhanst gas outlet, and the bottom is communicated with feed back pipe and feed back control valve, and 1. the bottom is provided with ash-valve.
The present invention adopts the method for above-mentioned gasification and the innovation part of device with positively effect to be: (1) with must use anthracite block coal or coke to compare as the water at atmospheric pressure producer gas generator of raw material, this technology is raw material with fine coal or coke breeze, this not only greatly reduces cost, has also opened up new way for fine coal or coke breeze utilization.(2) the present invention's design has inertial separator, upward ring casing L valve, thermopnore gasification urceolus, following ring casing L valve, fluidized-bed combustion promote structures such as inner core, the heat that fluidized-bed combustion lifting inner core produces is brought thermopnore gasification urceolus into by inner tube wall and red-hot coal charge and is provided heat for carry out gasification reaction in thermopnore gasification urceolus, and heat utilization ratio reaches 85%～92%.(3) the water at atmospheric pressure producer gas generator is owing to need to switch gas, so the mechanical means complexity is easy to wear, investment is big.And technology of the present invention, no handoff procedure, simple in structure, easy to maintenance, invest low.(4) water at atmospheric pressure producer gas generator, not gas making of temperature-rise period, production efficiency is low.The production efficiency height is carried out in technology gasification of the present invention, burning, heating continuously.(5) with oxygen-steam mixture be vaporized chemical continuous system water-gas technology as: fluidized-bed gasification Winkler, KRW and entrained flow gasification technology K-T stove, Texaco compare, although all aerobic (the oxygen-rich air)-water vapour of these technologies is vaporized chemical, but technology of the present invention is the easy part of gasification in the gasification of coal only, and the part fluidized-bed combustion of difficult gasification promotes inner core burned (using air), so the amount of its oxygen consumption-water vapour is low.(6) in the technology of the present invention, fluidized-bed combustion promotes the high-temperature flue gas of inner core generation at inertial separator and coal charge countercurrent flow, and the flue gas outflow temperature is low, the thermo-efficiency height.(7) promote the coal tar that the inner core unburn is most and heat up in fluidized-bed combustion, carried by High Temperature Gas and enter gasifying reactor, this coal tar promptly is that gasified raw material is again a thermal barrier, carries out solid circulation and transforms.
As seen from the above, characteristics of the present invention are: 1. three of the coal charge gasification big steps, both to heat, gasify and burnt respectively promote inner core in inertial separator, fluidized-bed gasification urceolus and fluidized-bed combustion and carry out, and eliminated the pollution of flue dust and destructive distillation volatile matter in the temperature-rise period; 2. the present invention designs separator, go up ring casing L valve, thermopnore gasifies urceolus, ring casing L valve, fluidized-bed combustion promote structures such as inner core down, and the heat that fluidized-bed combustion lifting inner core produces is brought the fluidized-bed gasification urceolus into by inner tube wall and red-hot coal charge provides heat for carry out gasification reaction in the fluidized-bed gasification urceolus; 3. process is carried out continuously, can realize high mechanization and unattended; 4. coal charge classification cycle continuous gasification has improved production efficiency greatly; 5. can utilize fine coal or coke breeze to be raw material, not only reduce cost, and make full use of fine coal or coke breeze resource; 6. product coal gas is the high quality raw material of oxygenatedchemicalss such as fine system alcohol ether based on CO and H2.
Description of drawings
Fig. 1 is technical process of the present invention and apparatus structure synoptic diagram
Fig. 2 is technical process of the present invention and apparatus structure A-A diagrammatic cross-section
Fig. 3 is technical process of the present invention and apparatus structure B-B diagrammatic cross-section
Among the figure: 1: ring-like coal feed point 2: separator 3: inner core sleeve pipe 4: upper ring casing L valve 5: upper ring casing L valve promotes gas entrance 6: fluidized gasification urceolus 7: fluidized bed combustion promotes inner core 8: lower ring casing L valve 9: lower ring casing L valve promotes gas entrance 10: air distribution plate 11: compressed air inlet 12: ash releasing tube 13: water sealed tank 14: waste gas outlet pipe 15: exhanst gas outlet 16: burnt gas separates 17: gas outlet tube 18: gas exit 19: coal gas separator 20: ash-valve 1. 21: feed back pipe 22: ash-valve 2. 23: feed back control valve 24: superheated vapour entrance
Embodiment
Below in conjunction with drawings and Examples the present invention is further detailed, present embodiment is to describe in further detail of the present invention, the present invention is not made any restriction.
Embodiment 1
Low volatile fine coal or anthracite fine coal are entered in the inertial separator 2 by ring-like coal inlet 1, after being 570 ℃～600 ℃ by 40 ℃～80 ℃ preheatings, enter in the ring casing L valve 4, promoting gas inlet 5 at last ring casing L valve promotes under the promotion of gas, enter in the fluidized-bed gasification urceolus 6, carry out gasification reaction by superheated vapour inlet 24 200 ℃～250 ℃ superheated vapour and the red-hot coal charges that enter in the fluidized-bed gasification urceolus 6, the coal gas that reaction produces is by carrying out gas solid separation in the gas outlet tube 17 input whirlwind coal gas separators 19, and the coal gas after the separation is through gas exit 18 outputs; The coal tar of gasification reaction does not enter the mouth the 9 promotion gas promotions that enter down by the following ring casing L valve promotion gas of gasification urceolus bottom, be pushed in the fluidized-bed combustion lifting inner core 7 and carry out combustion gasification, the coal tar of part unburn gasification enters in the inertial separator 2 with combustion gas flowing, isolated coal tar enters in the ring casing L valve 4 once more, promote at last ring casing L valve under the promotion gas promotion of gas inlet 5, be pushed into once more in the thermopnore gasification urceolus 6 and carry out the internal recycle gasification, the high-temp waste gas that the partial combustion coal tar produces heats coal charge with the coal charge countercurrent flow in inertial separator 2, sent in the combustion exhaust cyclonic separator 16 by waste gas outlet pipe 14 then, isolating waste gas is discharged by exhanst gas outlet 15; Combustion exhaust cyclonic separator 16 and coal gas separator 19 isolated fly coal or flying dust by ash-valve 1. 20, ash-valve 2. 22, feed back control valve 23 carries out outer circulation gasification or fly ash emission; The lime-ash that burning produces in fluidized-bed combustion lifting inner core 7 enters the water sealed tank 13 from the ash releasing tube 12 of bottom.
A kind of equipment that is used to realize fuild bed composite circle coal gasification method, it comprises ring-like coal inlet 1, separator 2, inner core sleeve pipe 3, last ring casing L valve 4, last ring casing L valve promotes gas inlet 5, fluidized-bed gasification urceolus 6, fluidized-bed combustion promotes inner core 7, last ring casing L valve 8, following ring casing L valve promotes gas inlet 9, air distribution plate 10, compressed air inlet 11, ash releasing tube 12, water sealed tank 13, waste gas outlet pipe 14, exhanst gas outlet 15, combustion exhaust separator 16, gas outlet tube 17, gas exit 18, coal gas separator 19, ash-valve 1. 20, feed back pipe 21, ash-valve 2. 22, feed back control valve 23, superheated vapour inlet 24, its device structure is:
A fluidized-bed combustion is set promotes inner core (7), be provided with fluidized-bed gasification urceolus (6) in its outer cover, be connected with inner core sleeve pipe (3) and separator (2) at its top, the bottom is connected with air distribution plate (10), compressed air inlet (11), ash releasing tube (12) and water sealed tank (13);
A fluidized-bed gasification urceolus (6) is set, and portion is arranged with fluidized-bed combustion and promotes inner core (7) within it, and outer top is connected with ring casing L valve (4), goes up ring casing L valve promotion gas inlet (5), gas outlet tube (17); Outer bottom is connected with down ring casing L valve (8), ring casing L valve promotes gas inlet (9), superheated vapour inlet (24) and feed back pipe (21) down; The top is connected with separator (2); The bottom is connected with air distribution plate (10) and compressed air inlet (11) and ash releasing tube (12) and water sealed tank (13);
A separator (2) is set, and its lower end is connected with fluidized-bed gasification urceolus (6) and inner core sleeve pipe (3) and fluidized-bed combustion and promotes inner core (7), and the upper end is provided with ring-like coal inlet (1), and the side is communicated with combustion exhaust separator (16) by waste gas outlet pipe (14);
A coal gas separator (19) is set, the one upper lateral part is communicated with fluidized-bed gasification urceolus (6) by gas outlet tube (17), the upper end is provided with gas exit (18), and the bottom is communicated with feed back pipe (21) and feed back control valve (23), and the bottom is provided with ash-valve 2. (22);
A combustion exhaust separator (16) is set, the one upper lateral part is connected with separator (2) by waste gas outlet pipe (14), the upper end is provided with exhanst gas outlet (15), and the bottom is communicated with feed back pipe (21) and feed back control valve (23), and the bottom is provided with ash-valve 1. (20).
Claims (4)
1. fuild bed composite circle coal gasification method, it is characterized in that coal charge is entered in the ring casing L valve (4) after by separator (2) preheating by ring-like coal inlet (1), the promotion gas that is promoted gas inlet (5) by last ring casing L valve pushes in the fluidized-bed gasification urceolus (6), the overheated steam that enters with overheated steam inlet (24) gasifies, wherein the coal tar of end gasification enters down in the ring casing L valve (8), the promotion gas that promotes gas inlet (8) by following ring casing L valve pushes in the fluidized-bed combustion lifting inner core (7), the pressurized air that enters with compressed air inlet (11) rises and carries out combustion gasification, wherein the coal tar of unburn gasification enters in the separator (2) with burning gas and separates, coal tar after the separation enters in the ring casing L valve (4) once more, and the promotion gas that promotes gas inlet (5) by last ring casing L valve pushes and carries out the internal recycle gasification in the fluidized-bed gasification urceolus (6) once more;
In fluidized-bed gasification urceolus (6), gasify the coal gas that produces by separating in gas outlet tube (17) the input coal gas separator (19), coal gas after the separation is by gas exit (18) output, after the separation fly coal or flying dust by feed back control valve (23) and ash-valve 2. (22) carry out that outer circulation flies gasification or flying dust discharges outward;
Promote in fluidized-bed combustion and to carry out high-temp waste gas that combustion gasification produces in the inner core (7) and send in the combustion exhaust separator (16) by waste gas outlet pipe (14) and separate, high-temp waste gas after the separation is by the outer discharging of exhanst gas outlet (15), after the separation fly coal or flying dust by feed back control valve (23) and ash-valve 1. (20) fly coal outer circulation gasification or flying dust discharges outward;
The lime-ash that burning produces in fluidized-bed combustion lifting inner core (7) is entered in the water sealed tank (13) by the ash releasing tube (12) of bottom.
2. fuild bed composite circle coal gasification method as claimed in claim 1 is characterized in that described coal charge is low volatile fine coal or anthracite fine coal.
3. fuild bed composite circle coal gasification method as claimed in claim 1, it is characterized in that coal charge is entered in the separator (2) by ring-like coal inlet (1), after being 570 ℃～600 ℃ by 40 ℃～80 ℃ preheatings, enter in the ring casing L valve (4), the promotion gas that is promoted gas inlet (5) by last ring casing L valve pushes in the fluidized-bed gasification urceolus (6), 200 ℃～250 ℃ the superheated vapour and the red-hot coal charge that are entered in the fluidized-bed gasification urceolus (6) by superheated vapour inlet (24) carry out the combustion gasification reaction, wherein, the coal tar of unburn gasification reaction promotes promotion gas that gas inlet (9) enters by the following ring casing L valve of fluidized-bed gasification urceolus (6) bottom and pushes fluidized-bed combustion and promote the pressurized air that enters with compressed air inlet (11) and air distribution plate (10) in the inner core (7) and rise and carry out fluidized gasification once more, wherein, unburned coal tar enters in the separator (2) with combustion gas flowing and separates, coal tar after the separation enters in the ring casing L valve (4) once more, and the promotion gas that promotes gas inlet (5) by last ring casing L valve pushes and carries out the internal recycle gasification in the fluidized-bed gasification urceolus (6) once more;
The coal gas that gasification produces in fluidized-bed gasification urceolus (6) is sent in the coal gas separator (19) by gas outlet tube (17) and is carried out gas solid separation, and the coal gas after the separation is exported by gas exit (18);
Promote the high-temp waste gas that the burning coal tar produces in the inner core (7) in fluidized-bed combustion and in separator (2), heat coal charge with the coal charge countercurrent flow, sent in the combustion exhaust separator (16) by waste gas outlet pipe (14) then and separate, the high-temp waste gas after the separation is discharged by exhanst gas outlet (15);
After in combustion exhaust separator (16) and coal gas separator (19), separating fly coal or flying dust by feed back control valve (23) and ash-valve 1. (20), ash-valve 2. (22) carry out outer circulation and fly to discharge outside gasification or the flying dust;
The lime-ash that burning produces in fluidized-bed combustion lifting inner core (7) is entered in the water sealed tank (13) by the ash releasing tube (12) of bottom.
4. equipment that is used to realize fuild bed composite circle coal gasification method, it comprises ring-like coal inlet (1), separator (2), inner core sleeve pipe (3), last ring casing L valve (4), last ring casing L valve promotes gas inlet (5), fluidized-bed gasification urceolus (6), fluidized-bed combustion promotes inner core (7), following ring casing L valve (8), following ring casing L valve promotes gas inlet (9), air distribution plate (10), compressed air inlet (11), ash releasing tube (12), water sealed tank (13), waste gas outlet pipe (14), exhanst gas outlet (15), combustion exhaust separator (16), gas outlet tube (17), gas exit (18), coal gas separator (19), ash-valve is (20) 1., feed back pipe (21), ash-valve is (22) 2., feed back control valve (23), superheated vapour inlet (24) is characterized in that:
A fluidized-bed combustion promotes inner core (7), is arranged with fluidized-bed gasification urceolus (6) outside it, and the top is connected with inner core sleeve pipe (3) and separator (2), and the bottom is connected with air distribution plate (10), compressed air inlet (11), ash releasing tube (12) and water sealed tank (13);
A fluidized-bed gasification urceolus (6) is arranged with fluidized-bed combustion and promotes inner core (7) in it, outer top is connected with ring casing L valve (4), goes up ring casing L valve promotion gas inlet (5), gas outlet tube (17); Outer bottom is connected with down ring casing L valve (8), ring casing L valve promotes gas inlet (9), superheated vapour inlet (24) and feed back pipe (21) down; The top is connected with separator (2); The bottom is connected with air distribution plate (10) and compressed air inlet (11) and ash releasing tube (12) and water sealed tank (13);
A separator (2), its lower end are connected with fluidized-bed gasification urceolus (6) and inner core sleeve pipe (3) and fluidized-bed combustion and promote inner core (7), and the upper end is provided with ring-like coal inlet (1), and the side is communicated with combustion exhaust separator (16) by waste gas outlet pipe (14);
A coal gas separator (19), the one upper lateral part is communicated with fluidized-bed gasification urceolus (6) by gas outlet tube (17), and the upper end is provided with gas exit (18), and the bottom is communicated with feed back pipe (21) and feed back control valve (23), and the bottom is provided with ash-valve 2. (22);
A combustion exhaust separator (16), the one upper lateral part is connected with separator (2) by waste gas outlet pipe (14), and the upper end is provided with exhanst gas outlet (15), and the bottom is communicated with feed back pipe (21) and feed back control valve (23), and the bottom is provided with ash-valve 1. (20).
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| CN101775313A (en) * | 2010-03-06 | 2010-07-14 | 太原理工大学 | Entrained flow gasifier |
| CN101942345A (en) * | 2010-02-10 | 2011-01-12 | 马鞍山科达洁能有限公司 | Coal gas production device and method |
| CN101760246B (en) * | 2010-01-15 | 2011-02-02 | 太原理工大学 | Biomass feeder for pressurized fluidized bed gasifier |
| CN102660343A (en) * | 2012-05-22 | 2012-09-12 | 太原理工大学 | Coal-bed gas non-catalytic deoxygenation process by utilizing dual-barrel moving-bed reactor |
| CN102786989A (en) * | 2012-08-15 | 2012-11-21 | 太原理工大学 | Biomass and coal fluidized bed co-gasification equipment |
| CN102786990A (en) * | 2012-08-15 | 2012-11-21 | 太原理工大学 | Biomass and coal fluidized bed co-gasification method |
| CN105647591A (en) * | 2016-04-01 | 2016-06-08 | 南京理工大学 | Solid fuel fluidized bed pyrolysis, gasification and combustion graded conversion device and conversion method |
| CN106367123A (en) * | 2016-11-14 | 2017-02-01 | 中国科学院广州能源研究所 | Gasification production method for high calorific value synthesis gas and device for realizing method |
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Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN101760246B (en) * | 2010-01-15 | 2011-02-02 | 太原理工大学 | Biomass feeder for pressurized fluidized bed gasifier |
| CN101942345A (en) * | 2010-02-10 | 2011-01-12 | 马鞍山科达洁能有限公司 | Coal gas production device and method |
| CN101775313A (en) * | 2010-03-06 | 2010-07-14 | 太原理工大学 | Entrained flow gasifier |
| CN102660343A (en) * | 2012-05-22 | 2012-09-12 | 太原理工大学 | Coal-bed gas non-catalytic deoxygenation process by utilizing dual-barrel moving-bed reactor |
| CN102660343B (en) * | 2012-05-22 | 2013-08-07 | 太原理工大学 | Coal-bed gas non-catalytic deoxygenation process by utilizing dual-barrel moving-bed reactor |
| CN102786989A (en) * | 2012-08-15 | 2012-11-21 | 太原理工大学 | Biomass and coal fluidized bed co-gasification equipment |
| CN102786990A (en) * | 2012-08-15 | 2012-11-21 | 太原理工大学 | Biomass and coal fluidized bed co-gasification method |
| CN102786989B (en) * | 2012-08-15 | 2013-11-06 | 太原理工大学 | Biomass and coal fluidized bed co-gasification equipment |
| CN105647591A (en) * | 2016-04-01 | 2016-06-08 | 南京理工大学 | Solid fuel fluidized bed pyrolysis, gasification and combustion graded conversion device and conversion method |
| CN105647591B (en) * | 2016-04-01 | 2019-03-05 | 南京理工大学 | Solid fuel fluidized bed thermal decomposition gasification combustion staged conversion device and method |
| CN106367123A (en) * | 2016-11-14 | 2017-02-01 | 中国科学院广州能源研究所 | Gasification production method for high calorific value synthesis gas and device for realizing method |
| CN106367123B (en) * | 2016-11-14 | 2021-10-19 | 中国科学院广州能源研究所 | Gasification production method of high-calorific-value synthesis gas and device for implementing method |
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