CN101338205A - Device for generating gas and fuel from solid combustible - Google Patents

Device for generating gas and fuel from solid combustible Download PDF

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Publication number
CN101338205A
CN101338205A CNA2008101391755A CN200810139175A CN101338205A CN 101338205 A CN101338205 A CN 101338205A CN A2008101391755 A CNA2008101391755 A CN A2008101391755A CN 200810139175 A CN200810139175 A CN 200810139175A CN 101338205 A CN101338205 A CN 101338205A
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China
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tar
gas
fuel
pipe
combustion gas
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CNA2008101391755A
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Chinese (zh)
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周升阳
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Individual
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Individual
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Priority to CNA2008101391755A priority Critical patent/CN101338205A/en
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Abstract

The invention relates to a gas and combustible oil generating device from solid combustible fuel, technology of which is characterized in that the combustible fuel is filled in a gasifier for the reverse incomplete combustion under the hypoxia condition to generate combustible gas and tar. Fuel gas is generated from the generated combustible gas after the dust removing and the high temperature cracking of the second time. Then, the fuel gas enters a main pipeline for the standby application after the temperature lowering, pressurized storing, high pressure liquefaction of the tar, the separation of the tar and highly precise filtering of the tar. The tar in the fuel gas is transformed in three steps of high temperature cracking, high pressure liquefaction and precise filtering. The tar content of the fuel gas entering the main pipeline is low. And the fuel gas belongs to clean fuel gas. Equipments comprises the gasifier, a dust removing high temperature cracking tar device, a temperature lowering device, a compressor, a kindling test air port, a gas storing liquefaction tar tank, a precise filtering tar device, etc. Fuel oil generates from the separated tar after the smelting and the distillation.

Description

But a kind of solid-state combustiblematerials generates the device of combustion gas and fuel oil
Technical field
But the present invention relates to the device that a kind of solid-state combustiblematerials generates combustion gas and fuel oil, combustiblesubstance is under the anoxybiotic condition, and oppositely incomplete combustion produces inflammable gas and tar, the tar that generates is smelted distillation again and can be produced fuel oil, the invention belongs to petrochemical industry.
Background technology
In recent years, country strengthens the support dynamics of development combustion gas, many solid-state combustiblematerials straw gasification stations have been built on some rural areas and farm, existing solid-state based on gasification of combustible material station exists that gas tar oil is removed thoroughly, problem such as low, the working cost height of blocking pipe, fuel gases calorific value easily, and these reasons cause some gasification stations to stop using, scrap.
Summary of the invention
The present invention overcomes the above-mentioned defective of prior art, but development provides that a kind of solid-state combustiblesubstance exempts to pulverize, fire grate anti-ly burns, dedusting thoroughly, tar filters that high pressure is supplied gas, calorific value height, solid-state based on gasification of combustible material device that working cost is cheap.
Implementation process of the present invention: with the combustiblesubstance vapourizing furnace of packing into, the reverse incomplete combustion of combustiblematerials produces inflammable gas and tar under the anoxybiotic condition.Pintsch process generation combustion gas again after the inflammable gas process fly-ash separator dedusting that produces; Combustion gas stores through the pressurization of cooling back.The tar that contains in the combustion gas is liquefied as the bottom of small droplets attached to gas-holder under the highly compressed condition, discharge tar through the coke discharging oil pipe, and through high precision filter tar device, what enter main pipe line has been exactly the combustion gas of cleaning again in combustion gas.Tar in the combustion gas is through Pintsch process, high-pressure liquefaction, three grades of conversions of secondary filter, and the gas tar oil content that enters main pipe line is very low, belongs to clean combustion gas.The major equipment that the present invention includes: vapourizing furnace, dedusting Pintsch process device, cooler, pneumatic plant, light gas testing mouth, gas storage liquefaction tar jar, secondary filter tar device etc.
The burner hearth that the present invention relates to vapourizing furnace is decided according to the shape of solid-state gasification substance, gasification substance is microscler, as maize straw, long waddy etc., can become rectangular parallelepiped to the chamber design of vapourizing furnace, gasification substance is shaped as bulk, can be designed to vapourizing furnace circular or square.
The fire grate that the present invention relates to vapourizing furnace is made with resistance to oxidation, resistant to elevated temperatures material, the fuel gases calorific value height that combustiblesubstance gasifies on special fire grate.
The dedusting Pintsch process device that the present invention relates to is totally enclosed, diameter 1--2 centimetre dedusting particle is housed, inlet pipe is below fly-ash separator, escape pipe is on fly-ash separator, dust is blocked by the dedusting particle, just dropped in the dust bucket, the dedusting particle can be to the pyrolytic gasification again of the tar in the combustion gas under the pyritous situation.
The cooler that the present invention relates to is the helical annular iron pipe that is placed in the pond, and high-temperature fuel gas flows in pipe, and heat is absorbed by mobile water.
The pneumatic plant that the present invention relates to is resistant to elevated temperatures supercharging equipment, and inlet mouth connects the air outlet of cooler, and the air outlet connects the examination burner, when treating that combustion gas can be lighted, import the inlet mouth of gas-holder, can be pressurized to 3-5 normal atmosphere to combustion gas by pneumatic plant, high pressure conditions reaches a high temperature, be stored in the gas-holder, the tar in the combustion gas is under the highly compressed effect, and temperature reduces gradually and is atomized into liquid state, on the gas storage tank skin, tar flows out through valve pipe to dirty, plays the purpose of separating tar.
The secondary filter tar device that the present invention relates to utilizes gas filter that tar is separated with combustion gas exactly, and is totally-enclosed gas filter, inlet pipe below, escape pipe in the above, the oil pipe that discharges of the coke is connected with threeway with inlet pipe, tar is from following outflow.
Description of drawings
Figure of description is the gasification furnace structure synoptic diagram
Embodiment
Be described further with specific examples in conjunction with the accompanying drawings:
According to the shape of solid-state combustiblesubstance, make vapourizing furnace 1,2 meters of the internal diameters of vapourizing furnace 1, width are 0.6 meter, and insulation layer thickness is 30 centimetres, and outside dimension length is 2: 1 with wide ratio.Inside puzzles with refractory brick, and air outlet and ash output hole are below fire grate.Fire grate is made with the material with refractory properties, and the space between fire grate and the fire grate is 3-5 centimetre.Dust filter 2 is the pyramid type of double headed roller point, make with metal, the air outlet in the above, inlet mouth below, the centre is diameter 1--2 centimetre a dedusting particle, the dedusting particle can carry out pyrolytic gasification again to the tar in the combustion gas under the pyritous situation.Combustion gas enters dust filter 2 by inlet pipe, and ashes is blocked by the dedusting particle and drops in the dust bucket.Cooler 3 is the spiral iron pipes that are placed in the water, and high-temperature fuel gas flows in the pipe the inside, and outside round-robin water works to absorb heat.Gas-holder 6 is a ferrous products, can be high pressure resistant, inlet mouth is 6 upper left of gas-holder, the air outlet is at upper right, gas-holder crouches and puts, discharge of the coke hydraulic fluid port under.During combustion gas process pneumatic plant 4, can be pressurized to 3-5 normal atmosphere, high pressure conditions reaches a high temperature, be stored in the gas-holder 6 after the combustion gas pressurization, the tar in the combustion gas is under the highly compressed effect, and temperature reduces gradually and is atomized into drop, on the gas storage tank skin, slowly flow to the gas-holder bottom, flow out, play the purpose of separating tar through valve pipe.Filtered tar device (7) be iron make, totally enclosed, the inner gas filter of installing, inlet pipe below, escape pipe in the above, the oil pipe that discharges of the coke is in the bottom, tar is emitted from following discontinuity.
According to the figure apparatus shown, with pipeline and ring flange 1,2,3,4,5,6,7 equipment are coupled together in order in order, the air outlet that the air outlet that the air outlet that the air outlet that the air outlet of vapourizing furnace 1 connects inlet mouth, the dust filter 2 of dust filter 2 connects the inlet mouth of cooler 3, cooler 3 connects inlet mouth, the pneumatic plant 4 of pneumatic plant 4 connects the inlet mouth of examination fire tube 5, examination fire tube 5 connects the inlet mouth of gas-holder 6, the air outlet of gas-holder 6 connects coke filter 7 inlet mouths, and coke filter 7 air outlets connect main pipe line.
Solid-state combustiblesubstance is put into vapourizing furnace 1, light from above, start pneumatic plant 4, solid-state combustiblesubstance will burn downwards, generate the pyritous combustion gas, the pyritous combustion gas enters the inlet mouth of fly-ash separator 2 under the effect of pneumatic plant 4, combustion gas is through the dedusting particle high-temperature once more after the cracking, enter cooler 3 from the air outlet outflow and lower the temperature, most of heat is taken away by the water around the cooler in the combustion gas, and combustion gas is flowed out from cooler 3 air outlets, enter pneumatic plant 4, combustion gas enters examination fire tube 5 after pressurizeing through pneumatic plant 4, at examination fire tube 5 places examination fire, when combustion gas can be lighted, open the air intake valve of gas-holder 6 again, begin to collect combustion gas.After operation for some time, open the put-focus fuel tap door of gas-holder 6 and the put-focus fuel tap door of combustion gas coke filter 7, emit tar.
Equipment is in service just to have only an electric motor that drives pneumatic plant 4 in running, and working cost is cheap; Fire grate place temperature height, the fire in a stove before fuel is added is prosperous, and the fuel gases calorific value of generation is just high; Solid-state combustiblesubstance can directly add, and need not pulverize; Dedusting is thorough; Tar filters; But high pressure is supplied gas; Calorific value height, working cost are cheap.The tar of producing is smelted and is become fuel oil.

Claims (7)

1, but a kind of solid-state combustiblematerials generates the device of combustion gas and fuel oil, its technical characterictic is: but the device of a kind of solid-state based on gasification of combustible material, generation combustion gas and fuel oil is made furnace chamber with lagging material exactly, fire grate is that a kind of material of high temperature resistance is made, the inflammable gas that produces is through dedusting, cooling, pressurization stores, separating tar, filtered tar, it is stand-by to enter main pipe line.Comprise: vapourizing furnace, fly-ash separator, cooler, pneumatic plant, gas-holder, filtered tar device etc.
2, according to claim 1, the fire grate material of vapourizing furnace is that anti-oxidant, resistant to elevated temperatures synthetic metallic substance is made.
3, according to claim 1, the gasification body of heater is to make according to the shape of combustiblesubstance.
4, according to claim 1, fly-ash separator is totally enclosed, and the dedusting particle of 1 centimetre of diameter is housed, and inlet pipe is below fly-ash separator, and escape pipe is on fly-ash separator.
5, according to claim 1, cooler is the spiral iron pipe that is placed in the water, and high-temperature fuel gas flows in the pipe the inside.
6, according to claim 1, pneumatic plant is resistant to elevated temperatures supercharging equipment, can be by pneumatic plant combustion gas sucking-off from vapourizing furnace, and be pressurized to 3-5 normal atmosphere, be stored in the gas-holder, under the highly compressed condition, tar in the combustion gas just is atomized into drop, on the gas storage tank skin, flow out through valve pipe the bottom that flows to gas-holder slowly again.
7, according to claim 1, the filtered tar device is to utilize gas filter tar is filtered, and is totally-enclosed gas filter, inlet pipe below, escape pipe in the above, the oil pipe that discharges of the coke is connected with threeway with inlet pipe.
CNA2008101391755A 2008-08-14 2008-08-14 Device for generating gas and fuel from solid combustible Pending CN101338205A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNA2008101391755A CN101338205A (en) 2008-08-14 2008-08-14 Device for generating gas and fuel from solid combustible

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Application Number Priority Date Filing Date Title
CNA2008101391755A CN101338205A (en) 2008-08-14 2008-08-14 Device for generating gas and fuel from solid combustible

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CN101338205A true CN101338205A (en) 2009-01-07

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101993735A (en) * 2010-12-03 2011-03-30 贝洪毅 Biomass dry gasification centralized air supply system
CN103450914A (en) * 2013-07-25 2013-12-18 易高环保能源研究院有限公司 Method for producing liquid fuel by performing fast pyrolysis on solid organic matters
CN112646610A (en) * 2020-12-18 2021-04-13 安徽香杨新能源科技发展股份有限公司 Gas conveying device for biomass gas production

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101993735A (en) * 2010-12-03 2011-03-30 贝洪毅 Biomass dry gasification centralized air supply system
CN101993735B (en) * 2010-12-03 2013-01-23 贝洪毅 Biomass dry gasification centralized air supply system
CN103450914A (en) * 2013-07-25 2013-12-18 易高环保能源研究院有限公司 Method for producing liquid fuel by performing fast pyrolysis on solid organic matters
CN112646610A (en) * 2020-12-18 2021-04-13 安徽香杨新能源科技发展股份有限公司 Gas conveying device for biomass gas production

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Open date: 20090107