CN2575098Y - Atmospheric molten bath gasifying equipment - Google Patents

Atmospheric molten bath gasifying equipment Download PDF

Info

Publication number
CN2575098Y
CN2575098Y CN 02244473 CN02244473U CN2575098Y CN 2575098 Y CN2575098 Y CN 2575098Y CN 02244473 CN02244473 CN 02244473 CN 02244473 U CN02244473 U CN 02244473U CN 2575098 Y CN2575098 Y CN 2575098Y
Authority
CN
China
Prior art keywords
feeder
coal
supercritical water
reactor
tube
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN 02244473
Other languages
Chinese (zh)
Inventor
王有素
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN 02244473 priority Critical patent/CN2575098Y/en
Application granted granted Critical
Publication of CN2575098Y publication Critical patent/CN2575098Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

The utility model relates to a continuous extracting reaction device for supercritical water of coal, which comprises a feeder 1, a reactor 2 connected below the feeder, a ball valve 3 connected with the reactor, a remnant coal tank 4 connected below the ball valve, and a remnant coal discharge valve 5 connected below the remnant coal tank. The utility model is characterized in the top part of the feeder 1 is inserted with a supercritical water injecting pipe 6. The extracting reaction can be carried out continuously by the utility model, and the utility model is suitable for industrial process. Because of the multivariate injection mode, the extracting reaction process can be reinforced, and the reaction speed is accelerated. The utility model has the advantages that extractant is cheap and facile, the extractant is non-toxic and harmless, supercritical water can be used in a circulating mode, the reaction condition is relative safe, and the utility model has no pollution to the environment.

Description

The supercritical water continuous extraction reaction unit of coal
Technical field
The utility model relates to the direct liquefaction equipment of coal, particularly a kind of supercritical water continuous extraction reaction unit of coal.
Technical background
Coal can carry out supercritical gas extraction and directly obtain oil fuel under certain temperature and pressure condition.Science researcher both domestic and external has successively carried out a large amount of research, has obtained some experiment achievements.The scientist of Britain in 1975 at first is extraction agent with toluene, carries out the extraction test of coal under the supercritical state of 350 ℃ and 10Mpa pressure.On July 1st, 1992, it is 87102560 that the Chinese patent communique discloses number of patent application.4, the authorization notification number is 1017251, name is called the patent of invention specification sheets of " continous process of supercritical gas extraction of coal and device thereof "; Though this patented technology has solved the problem of continuous extraction,, structure of reactor imperfection, reactant also flow from reactor and descend, and intermolecular effective collision rate is not high, thereby reaction effect is relatively poor, and speed is low; Use this method also to need to prepare equipment and the high-pressure pump handling equipment is supporting with coal slurry, so investment is big, the power consumption height.In addition, the extraction agent of use is inflammable and explosive, toxic, contaminate environment and the high organic solvent of price, under the higher reaction conditions of temperature, pressure, is prone to accidents, thereby has increased the difficulty that realizes suitability for industrialized production.
The content of invention
At the deficiency that prior art exists, the utility model provides a kind of reaction efficiency height, speed height, and environmentally safe, safe and reliable, less investment, energy consumption are low, is suitable for the supercritical water continuous extraction reaction unit of the coal of suitability for industrialized production.
The supercritical water continuous extraction reaction unit of coal described in the utility model, comprise feeder, be connected reactor below the feeder, be connected reactor ball valve, be connected residual coal jar below the ball valve, be connected the residual coal bleed valve below the residual coal jar, it is characterized in that being inserted with the supercritical water spray tube at the top of feeder.
The supercritical water continuous extraction reaction unit of described coal is characterized in that feeder top is cylinder, and the bottom is funnelform collapsible tube, and the outlet of collapsible tube connects trunnion, connects diffuser tube under the trunnion, is pipe connecting under the diffuser tube, and stretches into the top of reactor; The supercritical water spray tube inserts from the top of feeder, conical nozzle near and over against the outlet of collapsible tube; Vacuum breaker is connected the middle and upper part of feeder top cylinder.Supercritical water mixes with coal dust from the conical nozzle ejection of spray tube, has increased the effective collision between reactant molecule, thereby has strengthened reaction process, has accelerated speed of reaction.
The supercritical water continuous extraction reaction unit of described coal, its reactor top is cylinder, the bottom is the circular cone tube, sidewall is separately installed with filter disc, safety valve, thermowell and the mixed steam outlet pipe of powder of stainless steel moulding on the pipe connecting outlet of the feeder that stretches into cylinder top, on the mixed steam outlet pipe tensimeter is housed.The effect of filter disc is to stop that coal dust discharges from the mixed steam outlet pipe.Safety valve is to shield when the reactor pressure superelevation.Thermowell is used to insert the temperature in the thermometer Indicator Reaction device.
The filter inlet pipe that the supercritical water continuous extraction reaction unit of described coal, the middle and upper part of its residual coal jar are equipped with the powder of stainless steel moulding is connected with this filter disc, and supercutical fluid admission valve, tensimeter and the reducing valve of water is housed on the inlet pipe.Ball valve below opening reactor discharges before the residual coal, open admission valve feeds water in residual coal jar the supercutical fluid pressure in raising jar earlier, make in itself and the reactor pressure near or equate, open ball valve again and fall in the residual coal jar by the residual coal in the reactor; Before residual coal bleed valve below opening residual coal jar discharges residual coal, close ball valve earlier, after open reducing valve and emit gas in the residual coal jar, filter stops that residual coal emits with gas, the pressure in jar is opened residual coal bleed valve again and is discharged residual coal after reducing.
The utility model can make extractive reaction carry out continuously, is suitable for suitability for industrialized production; Changeable spray regime has been strengthened the extractive reaction process, has accelerated speed of reaction.The extraction agent that uses is cheap and easy to get, nontoxic, can recycle supercritical water, and reaction conditions is comparatively safe, environmentally safe; The utility model does not need coal slurry to prepare equipment and the high-pressure pump e Foerderanlage is supporting, and less investment, energy consumption are low.
Description of drawings
Fig. 1 is an organigram of the present utility model.
Embodiment
Referring to Fig. 1, the supercritical water fluid of high-voltage high-speed is from the conical nozzle ejection of the supercritical water spray tube 6 that is contained in feeder 1 top, carry out effective hybrid reaction at collapsible tube 14 places and from the vacuum breaker 7 automatic 80-100 purpose coal dusts that suck, and carry out extruding reaction by trunnion 15 at a high speed, continue to flow through diffuser tube 16 and pipe connecting 17 spurted into top and is equipped with in the reactor 2 of safety valve 9 and thermowell 10, produce violent turbulent flow owing to enter the fluid of reactor 2 from pipe connecting 17, the supercritical extraction reaction is proceeded, and separated thereupon; The mixture of supercritical water extraction agent and isolated vaporized fuel oil, passes filter disc 8 and enters separator from the mixed steam outlet pipe 11 on top after gravity separation with residual coal; Before the residual coal of ball valve 3 dischargings below opening reactor 2, open the admission valve 20 that is contained on the steam inlet pipe 21 earlier and in residual coal jar 4, feed high-pressure water vapor with the pressure in the jar that raises, tensimeter 12 readings on the reading that makes the tensimeter 19 that is installed on the steam inlet pipe 21 and the reactor mixed steam outlet pipe 11 near or when equating, open ball valve 3 again, residual coal is put into residual coal jar 4; Before the residual coal of residual coal bleed valve 5 dischargings below opening residual coal jar 4, close ball valve 3 earlier, after open reducing valve 20 and emit gas in the residual coal jar 4, filter 13 stops that residual coal emits with gas, after pressure in jar reduces, open the residual coal of residual coal bleed valve 5 dischargings again.
The utility model volume is little, but can handle a large amount of solid coal dusts continuously, during suitability for industrialized production, and can be with multiple devices production in parallel.

Claims (4)

1, the supercritical water continuous extraction reaction unit of coal, comprise feeder (1), be connected reactor (2) below the feeder, be connected reactor ball valve (3), be connected residual coal jar (4) below the ball valve, be connected the residual coal bleed valve (5) below the residual coal jar, it is characterized in that being inserted with supercritical water spray tube (6) at the top of feeder (1).
2, the supercritical water continuous extraction reaction unit of coal according to claim 1, it is characterized in that feeder (1) top is cylinder, the bottom is funnelform collapsible tube (14), the outlet of collapsible tube connects trunnion (15), connect diffuser tube (16) under the trunnion, be pipe connecting (17) under the diffuser tube, and stretch into the top of reactor (2); Supercritical water spray tube (6) inserts from the top of feeder (1), conical nozzle near and over against the outlet of collapsible tube (14); Vacuum breaker (7) is connected the middle and upper part of feeder (1) top cylinder.
3, the supercritical water continuous extraction reaction unit of coal according to claim 1, it is characterized in that reactor (2) top is cylinder, the bottom is the circular cone tube, sidewall is separately installed with filter disc (8), safety valve (9), thermowell (10) and mixed steam outlet pipe (11) on pipe connecting (17) outlet of the feeder that stretches into cylinder top (1), and tensimeter (12) is housed on the mixed steam outlet pipe.
4, the supercritical water continuous extraction reaction unit of coal according to claim 1, the middle and upper part that it is characterized in that residual coal jar (4) is equipped with filter (13), inlet pipe (21) is connected with this filter disc (13), and supercutical fluid admission valve (18), tensimeter (19) and the reducing valve (20) of water is housed on the inlet pipe (21).
CN 02244473 2002-10-17 2002-10-17 Atmospheric molten bath gasifying equipment Expired - Fee Related CN2575098Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 02244473 CN2575098Y (en) 2002-10-17 2002-10-17 Atmospheric molten bath gasifying equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 02244473 CN2575098Y (en) 2002-10-17 2002-10-17 Atmospheric molten bath gasifying equipment

Publications (1)

Publication Number Publication Date
CN2575098Y true CN2575098Y (en) 2003-09-24

Family

ID=33716353

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 02244473 Expired - Fee Related CN2575098Y (en) 2002-10-17 2002-10-17 Atmospheric molten bath gasifying equipment

Country Status (1)

Country Link
CN (1) CN2575098Y (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105349183A (en) * 2015-11-06 2016-02-24 中国科学院山西煤炭化学研究所 Method and device for preparing active carbon and byproducts of combustion gas and tar through conversion of coal in supercritical water
CN115228137A (en) * 2022-08-17 2022-10-25 明士新材料有限公司 Modularized continuous extraction separation method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105349183A (en) * 2015-11-06 2016-02-24 中国科学院山西煤炭化学研究所 Method and device for preparing active carbon and byproducts of combustion gas and tar through conversion of coal in supercritical water
CN105349183B (en) * 2015-11-06 2017-11-17 中国科学院山西煤炭化学研究所 The method and apparatus that coal conversion in supercritical water prepares activated carbon by-product combustion gas simultaneously and tar
CN115228137A (en) * 2022-08-17 2022-10-25 明士新材料有限公司 Modularized continuous extraction separation method

Similar Documents

Publication Publication Date Title
CN103112831B (en) Liquid sulphur degassing device and liquid sulphur degassing method
CN2516218Y (en) Coal supercritical CO2 continuous extraction reaction device
CN2575098Y (en) Atmospheric molten bath gasifying equipment
CN201545792U (en) Safe separation and recovery unit for acetylene and carbide slag in dry acetylene generator
CN113083145A (en) Solid material multistage jet high-pressure continuous feeding device
CN202181892U (en) Well opening simple gas-liquid separating metering device
CN208695276U (en) A kind of flotation device that recovery efficiency is high
CN202866864U (en) Pulp shooting machine dust-clearing system
CN104815530A (en) Jet-type membrane-filtering fine-desulfuration device suitable for refinery plant
CN203159222U (en) Liquid sulfur degassing device
CN201147723Y (en) Micro-bubble jet flotation machine
CN204162411U (en) Dry hydrogen production equipment
CN2544793Y (en) Negative pressre ammonia rear gas safety environmetally friendly recovery device
CN207342942U (en) A kind of desulfurization injector
CN206676189U (en) A kind of solvent tail gas retracting device
CN202876769U (en) Cyclic catalysis environment-friendly equipment
CN215388517U (en) Device for improving recovery rate of dimethyl carbonate device tail gas materials
CN203319965U (en) Hydration reactor for processing coalbed methane
CN2341103Y (en) Coal powder sprayer for blast furnace
CN202215452U (en) Device for preventing chilling water pump from cavitating in coal-based methanol to propylene process
CN215742366U (en) Gas-liquid separation device suitable for coal mine gas power generation
CN218890357U (en) Tail gas EG recycling structure of slurry tank in polyester workshop
CN212152405U (en) Normal temperature and pressure ammonia leaching tank
CN201815125U (en) Novel loxygen discharge evaporator
CN203944160U (en) A kind of online degasser of pipeline fluid

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee