CN103113918A - Water gas generator - Google Patents

Water gas generator Download PDF

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Publication number
CN103113918A
CN103113918A CN2013100351770A CN201310035177A CN103113918A CN 103113918 A CN103113918 A CN 103113918A CN 2013100351770 A CN2013100351770 A CN 2013100351770A CN 201310035177 A CN201310035177 A CN 201310035177A CN 103113918 A CN103113918 A CN 103113918A
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CN
China
Prior art keywords
gas
coal
water
liquid separation
generator
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.)
Pending
Application number
CN2013100351770A
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Chinese (zh)
Inventor
吴震宇
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.)
Wujiang Xinjincheng Stainless Steel Products Co Ltd
Original Assignee
Wujiang Xinjincheng Stainless Steel Products Co Ltd
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 Wujiang Xinjincheng Stainless Steel Products Co Ltd filed Critical Wujiang Xinjincheng Stainless Steel Products Co Ltd
Priority to CN2013100351770A priority Critical patent/CN103113918A/en
Publication of CN103113918A publication Critical patent/CN103113918A/en
Pending legal-status Critical Current

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Abstract

The invention provides a micro water gas generator. Water and coal are compounded to generate combustible gas. The micro water gas generator consists of a steam generator, a heat conduction ceramic heating and reacting plate, a gas-liquid separation cover, a gas-liquid separation cavity, a water gas outlet, a convolute combustor and an automatic coal feeder, wherein the steam generator supplies steam to the coal on the ceramic heating and reacting plate; gas produced from reaction enters the gas-liquid separation cavity through the gas-liquid separation cover for separation; part of combustible gas enters the convolute combustor for combusting and supplying the heat required by the steam generator; the coal is supplied continuously by the automatic coal feeder; and the produced combustible gas is led out from the water gas outlet. The advantage is that the combustible gas produced by the water gas generator is high in purity and good in integral economic benefit.

Description

Blue-gas generator
Technical field
The present invention relates to a kind of producer gas generator, especially blue-gas generator.
Background technology
Coal gasification in present producer gas generator is divided into dry distillation and two processes of gasification.Enter stove coal cinder (bituminous coal) at dry distillation section slow decreasing, the heating gas that rises with gasification section carries out directly and countercurrent exchange indirectly, through super-dry, preheating, dry distillation three phases, make the things such as fugitive constituent in coal cinder, moisture raise and progressively separate out with temperature, produce dry distillation coal gas and form semicoke, semicoke enters gasification section and is gasified totally.The heating gas that gasification section produces, 60-70% wherein goes out lower part outlet and draws, and is called lower coal gas, and 30-40% mixes with dry distillation coal gas through the dry distillation section in addition, and the outlet of top, mountain is drawn, and is called coal gas.
Several stages below the physical chemistry main transformerization that coal occurs in the dry distillation section mainly comprises:
1, drying stage (150 ℃): surface water, planar water evaporation in coal.
2, pre-heating stage (150-300 ℃): in the time of 150 ℃-300 ℃, emit crystal water when few, carbonic acid gas and hydrocarbon polymer in coal.In the time of 200 ℃-300 ℃, in coal, compound begins to decompose, and carbonic acid gas increases, and emits a small amount of tar.
3, the dry distillation stage (300-600 ℃): in the time of 300-400 ℃, coal begins to soften, and decomposites inflammable gas, the tar gas such as unsaturated hydrocarbons, methane, hydrogen; In the time of 400-450 ℃, decomposite in a large number tar gas; 500-600 ℃ does not substantially produce tar and forms semicoke.
Redox reaction when coal with gasification host (air, water vapor), complexity occurs in the gas section generates inflammable gas and the carbonic acid gas such as carbon monoxide, hydrogen, and the principal reaction process can represent with following a few prescription formulas:
1、C+O2=CO2+Q
2,2H2O (vapour)=2H2+Q2-Q
3、CO2+C=2CO-Q
4, H2O (vapour)+C=CO+H2-Q
5,2H2O (vapour)+C=CO2+2H2-Q
And present producer gas generator is mainly to maximize, and is not suitable for medium-sized and small enterprises and uses.
Summary of the invention
The invention provides a kind of miniature blue-gas generator.
a kind of blue-gas generator, become inflammable gas by water with the coalification symphysis, it is characterized in that by steam generator, thermal conductive ceramic reacting by heating dish, the gas-liquid separation cover, gas-liquid separation chamber, the water-gas export mouth, the convolution burner, automatically the device of delivering coal forms, steam generator supply water vapour is to the coal on the ceramic heat reaction tray, the gas that reaction generates is through the gas-liquid separation cover, entering gas-liquid separation chamber separates, the part inflammable gas enters the convolution burner and burns, the required heat of supply steam generator, coal continues supply by the device of automatically delivering coal, the inflammable gas water-gas export mouth that generates is derived.
Produce an effect has like this, and the inflammable gas purity that the Miniature water producer gas generator generates is higher, and whole is good in economic efficiency.
Description of drawings
Accompanying drawing is structural representation of the present invention.
Wherein: 1. the device of automatically delivering coal; 2. water-gas export mouth; 3. gas-liquid separation cover; 4. thermal conductive ceramic reacting by heating dish; 5. steam generator; 6. gas-liquid refrigerated separation chamber; 7. convolution burner.
Embodiment
The present invention will be further described below in conjunction with accompanying drawing: steam generator 5 supply water vapour are to the coal on ceramic heat reaction tray 4, the gas that reaction generates is through gas-liquid separation cover 3, entering gas-liquid separation chamber 6 separates, the part inflammable gas enters convolution burner 7 and burns, the required heat of supply steam generator, coal continues supply by the device 1 of automatically delivering coal, and derives in the inflammable gas water-gas export mouth 2 that generates.
In preferred version, water can first participate in the cooling of gas-liquid refrigerated separation chamber, realizes simultaneously heating up, and then imports steam generator.
In preferred version, it is anti-oxidant that the inner employing of burner hearth is coated with pottery, and with the calcium carbonate that adds 3~5% in coal cinder, can eliminate most of sulphur emissions.
Adopt producer gas generator of the present invention, can supply the artificial coal gas of 5-5000m3/ day, be applied to the places such as middle-size and small-size dining room, boiler, improve energy utilization rate, realize economizing on coal 30~50%, and decrease pollutes.

Claims (3)

1. blue-gas generator, become inflammable gas by water with the coalification symphysis, it is characterized in that by steam generator, thermal conductive ceramic reacting by heating dish, the gas-liquid separation cover, gas-liquid separation chamber, the water-gas export mouth, the convolution burner, automatically the device of delivering coal forms, steam generator supply water vapour is to the coal on the ceramic heat reaction tray, the gas that reaction generates is through the gas-liquid separation cover, entering gas-liquid separation chamber separates, the part inflammable gas enters the convolution burner and burns, the required heat of supply steam generator, coal continues supply by the device of automatically delivering coal, the inflammable gas water-gas export mouth that generates is derived.
2. blue-gas generator as claimed in claim 1 is characterized in that water can first participate in the cooling of gas-liquid refrigerated separation chamber, realizes simultaneously heating up, and then imports steam generator.
3. blue-gas generator as claimed in claim 1, is characterized in that the inner employing of burner hearth is coated with pottery anti-oxidant, and with the calcium carbonate that adds 3~5% in coal cinder.
CN2013100351770A 2013-01-30 2013-01-30 Water gas generator Pending CN103113918A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2013100351770A CN103113918A (en) 2013-01-30 2013-01-30 Water gas generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2013100351770A CN103113918A (en) 2013-01-30 2013-01-30 Water gas generator

Publications (1)

Publication Number Publication Date
CN103113918A true CN103113918A (en) 2013-05-22

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2013100351770A Pending CN103113918A (en) 2013-01-30 2013-01-30 Water gas generator

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109110730A (en) * 2018-09-11 2019-01-01 浙江工业职业技术学院 Power device for making for new-energy automobile

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1051752A (en) * 1989-11-17 1991-05-29 克鲁普克普斯有限公司 The method and apparatus of the raw gas of cooling segment oxidation
CN1168458A (en) * 1996-06-14 1997-12-24 三菱重工业株式会社 Steam generator
US20030083391A1 (en) * 2001-10-23 2003-05-01 Jahnke Fred C. Making fischer-tropsch liquids and power
CN101381608A (en) * 2007-09-07 2009-03-11 张远杰 Biomass gasifying machine
CN201261774Y (en) * 2008-06-22 2009-06-24 闫万河 Waste heat recovering fluidized bed gasification furnace
CN201265883Y (en) * 2008-04-19 2009-07-01 高礼根 Energy-saving environment-friendly gasification furnace
US20090221720A1 (en) * 2008-02-29 2009-09-03 Conocophillips Company Conversion of produced oxygenates to hydrogen or synthesis gas in a carbon-to-liquids process

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1051752A (en) * 1989-11-17 1991-05-29 克鲁普克普斯有限公司 The method and apparatus of the raw gas of cooling segment oxidation
CN1168458A (en) * 1996-06-14 1997-12-24 三菱重工业株式会社 Steam generator
US20030083391A1 (en) * 2001-10-23 2003-05-01 Jahnke Fred C. Making fischer-tropsch liquids and power
CN101381608A (en) * 2007-09-07 2009-03-11 张远杰 Biomass gasifying machine
US20090221720A1 (en) * 2008-02-29 2009-09-03 Conocophillips Company Conversion of produced oxygenates to hydrogen or synthesis gas in a carbon-to-liquids process
CN201265883Y (en) * 2008-04-19 2009-07-01 高礼根 Energy-saving environment-friendly gasification furnace
CN201261774Y (en) * 2008-06-22 2009-06-24 闫万河 Waste heat recovering fluidized bed gasification furnace

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109110730A (en) * 2018-09-11 2019-01-01 浙江工业职业技术学院 Power device for making for new-energy automobile

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Application publication date: 20130522