CN203904283U - Pressure reducing device used in continuous pressure-relief slagging of slag tapping pressurized gasifier - Google Patents
Pressure reducing device used in continuous pressure-relief slagging of slag tapping pressurized gasifier Download PDFInfo
- Publication number
- CN203904283U CN203904283U CN201420281938.0U CN201420281938U CN203904283U CN 203904283 U CN203904283 U CN 203904283U CN 201420281938 U CN201420281938 U CN 201420281938U CN 203904283 U CN203904283 U CN 203904283U
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- slag
- outer tube
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- relief
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- 239000002893 slag Substances 0.000 title claims abstract description 60
- 238000010079 rubber tapping Methods 0.000 title abstract description 10
- 238000002309 gasification Methods 0.000 claims description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 50
- 239000002002 slurry Substances 0.000 description 27
- 230000006837 decompression Effects 0.000 description 23
- 238000000034 method Methods 0.000 description 22
- 239000007789 gas Substances 0.000 description 18
- 238000006243 chemical reaction Methods 0.000 description 7
- 239000007788 liquid Substances 0.000 description 7
- 238000000926 separation method Methods 0.000 description 7
- 239000000203 mixture Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000007599 discharging Methods 0.000 description 4
- 238000013467 fragmentation Methods 0.000 description 4
- 238000006062 fragmentation reaction Methods 0.000 description 4
- 238000010791 quenching Methods 0.000 description 4
- 239000010797 grey water Substances 0.000 description 3
- 239000003818 cinder Substances 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000011010 flushing procedure Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241001391944 Commicarpus scandens Species 0.000 description 1
- 241001300078 Vitrea Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000001077 hypotensive effect Effects 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000013268 sustained release Methods 0.000 description 1
- 239000012730 sustained-release form Substances 0.000 description 1
- 230000026676 system process Effects 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Classifications
-
- 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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- Paper (AREA)
Abstract
The utility model discloses a pressure reducing device used in continuous pressure-relief slagging of a slag tapping pressurized gasifier. The pressure reducing device used in the continuous pressure-relief slagging of the slag tapping pressurized gasifier can be used for solving the problems of the existing slagging system that continuous slagging can not be realized, operation is cumbersome, the equipment investment is high and the reliability is poor. The pressure reducing device used in the continuous pressure-relief slagging of the slag tapping pressurized gasifier comprises an inner tube and an outer tube which are sheathed, wherein multiple pressure-relief holes are respectively formed in the inner tube and the outer tube, and the pressure-relief holes in the outer tube are connected with an exhaust tank by virtue of a pipeline and a throttle device. The pressure reducing device used in the continuous pressure-relief slagging of the slag tapping pressurized gasifier is simple and reliable, flexible and easy in operation, low in operation cost, energy-saving and cost-reducing, simple in system, low in equipment investment, high in reliability and long in service life.
Description
Technical field
The utility model relates to gasification field, specifically the continuous pressure release deslagging of a kind of slag tap pressurized-gasification furnace reliever.
Background technology
At present, pressurized-gasification furnace has been widely used in the industries such as chemical industry, metallurgy, machinery.According to the temperature of reaction in vapourizing furnace and lime-ash state, pressurized gasification furnace slag discharge can be divided into dry ash extraction and slag tap: when the melt temperature of gasification reaction temperature lower than lime-ash, lime-ash will be discharged with solid-state form; And when the melt temperature of vapourizing furnace temperature of reaction high pressure lime-ash, molten ash can unrestricted flow, lime-ash will be discharged with liquid form.Because pressurized-gasification furnace gasification reaction temperature is generally all higher, take coal gasifier as example, adopt the pressurized-gasification furnace of entrained flow gasification, the temperature of reaction in its vapourizing furnace is up to more than 1600 ℃, and lime-ash becomes molten state to discharge substantially.Current application widely pressurized entrained-bed coal gasifier generally adopts the form of slag tap.Adopt slag tap major advantage to be: because gasification reaction temperature is high, can guarantee that the carbonaceous material in raw material fully reacts gasification, guarantee high efficiency of carbon conversion; Meanwhile, lime-ash forms vitreum slag through Quench under high temperature fused state, and stable in properties, on almost not impact of environment; In addition, through Quench, form Vitrea slag and also can be used as cement blending agent or road construction material, further fully utilize.
Current pressurized-gasification furnace slag tap system is all the dreg removing system adopting with lock hopper reliever substantially, and this system exists the shortcoming and defect of the following aspects: 1. vapourizing furnace deslagging mode is carried out for being interrupted, and can not realize the tapping process of continous-stable; 2. adopt lock hopper system, need to respectively increase by one group of residual cake valve in lock hopper upstream and downstream, system easily breaks down; 3. lock hopper system is divided into collection slag, decompression, deslagging, cleaning, five processes of pressurising, and carries out reciprocation cycle, and operation and control system is complicated; 4. the investment of lock hopper dreg removing system and process cost are high, difficult in maintenance, and cost is high.5. lock hopper system process process is complicated, and energy consumption is high, and reliability is not high, and economy is poor.
Summary of the invention
The purpose of this utility model is in order to address the above problem, provide a kind of simple in structure, flexible operation is easy, facility investment is low, reliability is high, long service life, the continuous pressure release deslagging of slag tap pressurized-gasification furnace reliever that running cost is low, energy-saving and cost-reducing.
Technical scheme comprises the inner and outer tubes of suit, has a plurality of vents on described inner and outer pipe, and the vent on described outer tube is connected with exhaust tank with throttling set through pipeline.
The inwall of described inner tube is equipped with spiral tube sheet, along the vertical center line of spiral tube sheet, has 1 opening.
Described outer tube evenly has three row's vents vertically, and every row has three vents, uniform to being equilateral triangle along outer tube diameter.
Described inner tube evenly has 5-15 row vent vertically, and every row has 6 vents, uniform to being regular hexagon along outer tube diameter.
The aperture of the vent on described outer tube is 10～150mm; The aperture of the vent in described inner tube is 10～100mm, and the vent aperture of inner tube is less than the vent aperture of outer tube.
The aperture of described opening is 50～200mm, and the clearance control between inner tube and outer tube is at 50～150mm.
The utility model method is: the high-temperature slag that pressurized-gasification furnace generates enters vapourizing furnace bottom to carry out after water-bath Quench, send into again dregs breaker fragmentation (preferably slag is crushed to below 40mm), slag after fragmentation forms slag-water slurry and enters relief pipe, slag-water slurry is when by relief pipe pressure release, the mixture containing high pressure gas and a small amount of thin pulp water producing further sends into through throttling set that exhaust tank washs and gas-liquid separation after decompression, slag-water slurry after pressure release enters slag holding tank through expansion joint, finally enters dragveyer; The discharge pneumatic transmission of described exhaust tank inner top is toward torch, and the pulp water of bottom is sent into slag holding tank.
Slag-water slurry after described pressure release is first sent into after hydrocyclone carries out cyclonic separation and is sent into slag holding tank again through expansion joint, and the overflowing liquid that described hydrocyclone top overflows is also sent into slag holding tank.
Wash-down water is sent into respectively the outlet at bottom of hydrocyclone and the outlet at bottom of slag holding tank for flushing cinder after pressurization.
Described relief pipe comprises the inner and outer tubes of suit, and the inwall of described inner tube is equipped with spiral tube sheet, along the vertical center line of spiral tube sheet, has 1 opening; On described inner and outer pipe, have a plurality of vents, the vent on described outer tube is connected with exhaust tank with throttling set through pipeline; Described slag-water slurry is the rapid pressure release decompression in descending along spiral tube sheet and opening spiral thereof in the inner tube of relief pipe, during pressure release, produce containing high pressure gas and a small amount of thin slag-water slurry first by after the vent in inner tube and the decompression of the vent on outer tube, after pipeline and throttling set are further depressurized, send into exhaust tank again, the slag-water slurry after pressure release enters expansion joint.
Contriver conducts in-depth research for existing pressurized-gasification furnace intermittent type pressure release tapping process, find that pressure leak process is the problem place that cannot carry out continuous discharging slag, can be the key addressing the above problem to the slag sustained release pressure from pressurized-gasification furnace, therefore, applicant improves pressurized-gasification furnace pressure release tapping process, first the slag of the furnace bottom of autopneumatolysis in the future carries out fragmentation, then disintegrating slag is sent in relief pipe, when utilizing the special construction of relief pipe and connected device that slag is fallen in relief pipe, carry out pressure release, the mixture containing high pressure gas and a small amount of thin pulp water producing during pressure release through throttling set further send into after decompression exhaust tank wash with gas-liquid separation after discharge, thereby realize the object of pressure release.
Because continuous relief pipe is Fatigue equipment, for assurance device continous-stable reliability service, described relief pipe can take 1 to open 1 standby collocation form, once the relief pipe moving, break down and maybe can not realize decompression object, be switched to immediately standby relief pipe, the relief pipe of fault switches system and overhaul accordingly.
Described exhaust tank can wash with separated the mixture containing high pressure gas and a small amount of thin pulp water of sending here, and gas is discharged by top, and slag-water slurry is discharged by bottom.
Described relief pipe adopts double-layer sleeve structure, and inner tube is provided with spiral tube sheet, along the vertical center line of spiral tube sheet, has opening.On described inner and outer pipe, have a plurality of vents, the vent on described outer tube is connected with exhaust tank with throttling set through pipeline.When high pressure slag-water slurry (the solid-liquid-gas three phase mixture that comprises slag, water and the dissolved under pressure high pressure gas in pulp water) is when through relief pipe, along spiral tube sheet in inner tube and opening thereof, fall, in dropping process, spiral tube sheet in inner tube plays spiral depressurization to high pressure slag-water slurry on the one hand, has delayed the Negotiation speed of pulp water; On the other hand, the mixture of the high pressure gas that in slag-water slurry, decompression discharges and a small amount of thin pulp water can be discharged along the vent of inner tube, interstitial diffusion through inner and outer pipe forms once decompression, and then send into pipeline through the decompression of throttling set formation secondary through the vent of outer tube, the mixture containing high pressure gas and a small amount of thin pulp water producing during decompression sends into exhaust tank washing after the further decompression of throttling set and gas-liquid separation discharges, and has finally played effect and the object of the continuous pressure release decompression of high pressure slag-water slurry.
Described throttling set can be restriction orifice or the pressure regulator valve of one or more series connection.
Further, preferably the vent quantity of inner tube is more than the vent of outer tube, and the aperture of the vent of inner tube is less than the vent aperture of outer tube, can improve like this effect of decompression.In order to guarantee even pressure release, on outer tube vent should along outer tube axially evenly have three row's vents, every row has three vents, uniform to being equilateral triangle along outer tube diameter.And inner tube evenly has 5-15 row vent vertically, every row has 6 vents, uniform to being regular hexagon along outer tube diameter, specifically can according to different pressure releases, require to control size and the row of vent in inner tube, the vent of described inner tube and the relief pipe of outer tube be not preferably on same horizontal plane.By being arranged in the position of inner and outer pipe vent, the restriction in pore size, quantity and inner and outer pipes gap, can at utmost guarantee the optimal effectiveness of pressure release to improve pressure release efficiency.
The utility model can be decompressed to 0.1～0.5MPaG continuously by the high pressure slag-water slurry of vapourizing furnace internal pressure 1.0～6.5MPaG, thereby realizes continuous discharging slag process.In order to guarantee stability and the reliability of depressurized system, described relief pipe adopts 1 to open 1 standby form.
Beneficial effect:
1. adopt the utility model device can cancel lock hopper system, cancel solid residual cake valve expensive and that be easy to break down, dreg-locking hopper recycle pump and slag water cooler have been cancelled simultaneously, the intermittent type decompression tapping process changing is in the past continuously decompression tapping process, has solved the variety of issue that intermittent type decompression brings.
2. reduce equipment investment cost and process cost, reduced maintenance cost, made operation and control simpler, reduced the failure rate of dreg removing system, improved stability and the reliability of gasification installation operation.
3. utilize exhaust tank relief pressure, collect the waste gas producing in decompression process, by washing separation, make pulp water separated with non-condensable gas, the waste gas that decompression process produces is directly sent to torch burning discharge, without poisonous pollution exhaust gas emission, process environmental protection, operational safety.
4. the simplicity of design of relief pipe is ingenious, facility investment is low, pressure release is effective, controllability is high, coordinates exhaust tank can effectively realize the continuous release of pressure, can be used for the continuous discharging slag under gasification industry pressurization slag tap operating mode.
Accompanying drawing explanation
Fig. 1 is the utility model apparatus structure schematic diagram.
Fig. 2 is the utility model relief pipe A-A diagrammatic cross-section;
Fig. 3 is the B portion enlarged view in Fig. 1.
Fig. 4 is that the utility model device is for the schematic flow sheet of vapourizing furnace deslagging technique.
Wherein: 1-pressurized-gasification furnace; 2-dregs breaker; 3-relief pipe, 3.1-outer tube, 3.2-inner tube, 3.3-spiral tube sheet, 3.4-outer tube vent, 3.5-inner tube vent, 3.6-opening; 4-expansion joint; 5-hydrocyclone; 6-slag holding tank; 7-dragveyer; 8-slag waggon; 9-throttling set; 10-exhaust tank; 11-grey water pump; 12-washpipe; 13-pulp water pump.
Embodiment
Below in conjunction with accompanying drawing, the utility model is further explained to explanation:
With reference to Fig. 1 and Fig. 2, the utility model relief pipe 3 comprises inner tube 3.2 and the outer tube 3.1 of suit, on described inner and outer pipe 3.2,3.1, has a plurality of vents, and the outer tube vent 3.4 on described outer tube 3.1 is connected with throttling set 9 through pipeline.The inwall of described inner tube 3.2 is equipped with spiral tube sheet 3.3, vertical center line along spiral tube sheet has 1 opening 3.6 (aperture is 50～200mm), the helical channel that the high pressure slag-water slurry falling can form along above-mentioned spiral tube sheet and opening 3.6 rotations thereof are descending, extend the whereabouts stroke of high pressure slag-water slurry under the interior unit height of relief pipe 3, played the effect of spiral decompression.Described outer tube 3.1 evenly has three row's vents vertically, and every row has three outer tube vents 3.4, is radially equilateral triangle uniform along outer tube 3.1.Described inner tube 3.2 evenly has 5-15 row vent vertically, and every row has 6 inner tube vents 3.5, uniform to being regular hexagon along outer tube diameter.The aperture of the outer tube vent 3.4 on described outer tube 3.1 is 10～150mm; The aperture of the inner tube vent 3.5 in described inner tube 3.2 is 10～100mm.The gap L that inner tube 3.2 and outer tube are 3.1 is controlled at 50～150mm, the aperture of the little outer tube vent 3.4 in aperture of inner tube vent 3.5.
With reference to Fig. 3 and Fig. 4, the annexation of the utility model during for the dreg removing system of pressurized-gasification furnace is: the pulp water outlet of pressurized-gasification furnace 1 is connected with dregs breaker 2, relief pipe 3, expansion joint 4, hydrocyclone 5, slag holding tank 6 and dragveyer 7 successively, described relief pipe 3 is also connected with exhaust tank 10 through throttling set 9, described exhaust tank 10 outlet at bottom and the top exit of hydrocyclone be also connected with slag holding tank 6.The outlet at bottom of the outlet at bottom of described hydrocyclone 5 and slag holding tank 6 is all established washpipe 12, and described washpipe 12 is connected with grey water pump 11 through pipeline.The non-condensable gas outlet of described slag holding tank 6 is also connected with exhaust tank 10, and the downward inclination angle a of the washpipe 12 of described slag holding tank 6 bottoms is 15～60 degree (seeing Fig. 3).
Technological process:
The slag that pressurized-gasification furnace 1 pyroreaction of 1.0～6.5MPaG generates drops into vapourizing furnace 1 bottom to carry out after water-bath Quench, bulk slag is crushed to and is less than after 40mm through dregs breaker 2, disintegrating slag enters in the relief pipe 3 being connected with vapourizing furnace bottom with current (being called for short high pressure slag-water slurry), through the continuous pressure release of relief pipe 3, be decompressed to after 0.1～0.5MpaG, enter into the expansion joint 4 of relief pipe 3 bottoms and slow down the reactive force of whereabouts, then slag-water slurry is sent into hydrocyclone 5 together, under the effect of hydrocyclone 5, pulp water layering, slag-water slurry is by hydrocyclone bottom slag input holding tank 6, the overflowing liquid at hydrocyclone 5 tops is also sent into slag holding tank 6 by top exit, last slag-water slurry is discharged into dragveyer 7 by conduit by slag after being cooled and being cooled to 50～80 ℃, and pull out to slag waggon 8 and be sent to out-of-bounds by dragveyer 7, drag for the slag bath water reuse after pulp water pump 13 is sent into lower procedure processing after slag.
Hydrocyclone 5 outlet at bottoms are connected with the low temperature buck of 40～60 ℃ as wash-down water that gasification installation follow-up system is sent here, after grey water pump 11 pressurizations, through washpipe 12, send into respectively the outlet at bottom place of hydrocyclone 5 and slag holding tank 3, for flushing cinder and cooling down high-temperature slag-water slurry, the slag-water slurry that assurance is discharged by slag holding tank 6 is cooled and is cooled to 50～80 ℃.
The decompression process of relief pipe 3 is as follows: when the high pressure slag-water slurry after fragmentation enters relief pipe 3, along the helical channel forming between inner tube 3.2 and spiral tube sheet 3.3 and the vent on spiral tube sheet 3.6, fall, in dropping process, high pressure slag-water slurry rapid depressurization.Meanwhile, because relief pipe 3 is sleeve structure, the tube wall of inner and outer pipes 3.2,3.1 all evenly has vent, the high pressure gas that discharge during the pressure release of high pressure slag-water slurry and a small amount of thin pulp water are discharged through inner tube vent 3.5 and the outer tube vent on outer tube 3.1 3.4 of inner tube 3.2 successively, due to the current limliting hypotensive effect of vent, also make along the descending rapid pressure release of high pressure slag-water slurry of relief pipe 3.The high pressure gas of being discharged by the outer tube vent 3.4 of outer tube 3.1 and a small amount of thin pulp water are sent into exhaust tank 10 after being connected with the further step-down of pipeline of throttling set 9, the pressure that relief pipe 3 decompressions are released discharges by exhaust tank 10, finally realizes decompression and the pressure release object of high pressure pulp water.Exhaust tank 10 can be a column plate type container, the high pressure gas of discharging from relief pipe 3 and a small amount of thin pulp water are washed from the process water of out-of-bounds sending here exhaust tank 10, at exhaust tank 10 tops after vapor-liquid separating device separation, gas is sent to torch burning discharge, and isolated slag-water slurry is delivered to slag holding tank 6 by outlet at bottom through back of pipeline.In addition, the non-condensable gas in tank holding tank 6 also can be sent into exhaust tank 10 through non-condensable gas outlet and wash separation.
By above device and measure, played the effect of the continuous pressure release decompression of high pressure slag-water slurry, finally realized continuous pressure release and the deslagging object of the pressurized-gasification furnace of slag tap.
Claims (6)
1. the continuous pressure release deslagging of a slag tap pressurized-gasification furnace reliever, the inner and outer tubes that comprise suit, it is characterized in that, on inner and outer pipe, have a plurality of vents described in described relief pipe, the vent on described outer tube is connected with exhaust tank with throttling set through pipeline.
2. the continuous pressure release deslagging of slag tap pressurized-gasification furnace as claimed in claim 1 reliever, is characterized in that, the inwall of described inner tube is equipped with spiral tube sheet, along the vertical center line of spiral tube sheet, has 1 opening.
3. the continuous pressure release deslagging of slag tap pressurized-gasification furnace as claimed in claim 1 or 2 reliever, is characterized in that, described outer tube evenly has three row's vents vertically, and every row has three vents, uniform to being equilateral triangle along outer tube diameter.
4. the continuous pressure release deslagging of slag tap pressurized-gasification furnace as claimed in claim 1 or 2 reliever, is characterized in that, described inner tube evenly has 5-15 row vent vertically, and every row has 6 vents, uniform to being regular hexagon along outer tube diameter.
5. the continuous pressure release deslagging of slag tap pressurized-gasification furnace as claimed in claim 1 reliever, is characterized in that, the aperture of the vent on described outer tube is 10～150mm; The aperture of the vent in described inner tube is 10～100mm, and the aperture of inner tube vent is less than the aperture of outer tube vent.
6. the continuous pressure release deslagging of slag tap pressurized-gasification furnace as claimed in claim 2 reliever, is characterized in that, the aperture of described opening is 50～200mm, and the clearance control between inner tube and outer tube is at 50～150mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420281938.0U CN203904283U (en) | 2014-05-29 | 2014-05-29 | Pressure reducing device used in continuous pressure-relief slagging of slag tapping pressurized gasifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420281938.0U CN203904283U (en) | 2014-05-29 | 2014-05-29 | Pressure reducing device used in continuous pressure-relief slagging of slag tapping pressurized gasifier |
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| Publication Number | Publication Date |
|---|---|
| CN203904283U true CN203904283U (en) | 2014-10-29 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420281938.0U Expired - Lifetime CN203904283U (en) | 2014-05-29 | 2014-05-29 | Pressure reducing device used in continuous pressure-relief slagging of slag tapping pressurized gasifier |
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| Country | Link |
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| CN (1) | CN203904283U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110567261A (en) * | 2019-09-25 | 2019-12-13 | 河南心连心化学工业集团股份有限公司 | gasification ash drying device and method for four-nozzle water-gas entrained flow bed |
| CN110713847A (en) * | 2019-10-25 | 2020-01-21 | 华北理工大学 | Gasification device and method for preventing biomass fuel from coking |
-
2014
- 2014-05-29 CN CN201420281938.0U patent/CN203904283U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110567261A (en) * | 2019-09-25 | 2019-12-13 | 河南心连心化学工业集团股份有限公司 | gasification ash drying device and method for four-nozzle water-gas entrained flow bed |
| CN110567261B (en) * | 2019-09-25 | 2023-11-21 | 河南心连心化学工业集团股份有限公司 | Gasification ash drying device and method of four-nozzle water gas type entrained flow bed |
| CN110713847A (en) * | 2019-10-25 | 2020-01-21 | 华北理工大学 | Gasification device and method for preventing biomass fuel from coking |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20141029 |
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| CX01 | Expiry of patent term |