CN2723459Y - Gas burning purifier - Google Patents

Gas burning purifier Download PDF

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Publication number
CN2723459Y
CN2723459Y CN 200420070805 CN200420070805U CN2723459Y CN 2723459 Y CN2723459 Y CN 2723459Y CN 200420070805 CN200420070805 CN 200420070805 CN 200420070805 U CN200420070805 U CN 200420070805U CN 2723459 Y CN2723459 Y CN 2723459Y
Authority
CN
China
Prior art keywords
gas
water
storage
storehouse
enters
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 200420070805
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Chinese (zh)
Inventor
杨文海
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.)
Guangzhou Sinobaron Environmental Protection & Heating Power Equipment Co Ltd
Original Assignee
Guangzhou Sinobaron Environmental Protection & Heating Power Equipment 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 Guangzhou Sinobaron Environmental Protection & Heating Power Equipment Co Ltd filed Critical Guangzhou Sinobaron Environmental Protection & Heating Power Equipment Co Ltd
Priority to CN 200420070805 priority Critical patent/CN2723459Y/en
Application granted granted Critical
Publication of CN2723459Y publication Critical patent/CN2723459Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses a gas burning purifier, comprising an air intake duct, a water-sealed condensation storage, a whirlwind isolation storage, an air/water isolation storage, a coarse filtration storage, and a fine filtration storage and an outlet duct, which are all connected by the pipe in order, wherein the gas in the water-sealed condensation storage is condensed after passing the water-sealed face. The gas of the straw runs under positive pressure in the gas burning purifier; the gas enters through the intake pipe, passes through the water-sealed face of the water-sealed condensation storage to be washed and prevented from running back, and enters into the condensation storage from the top down to be condensed. The condense gas enters into the whirlwind isolation storage for water, gas, and dust separation, enters into the air/water valve isolation storage through the pipeline for removing part of moisture and tar, enters into the coarse filtration storage for further absorbing and filtering moisture and tar of the gas, enters into the fine filter storage, and runs through the fine filter material to exhaust the clean flammable gas which is exhausted through the outlet duct and conveyed to the gas cylinder or the user. The utility model is suitable for purifying the concentration gasified gas from the straw of the countryside, the ranch and the farm.

Description

A kind of gas cleaning device
Technical field
The utility model relates to a kind of gas cleaning device, relates in particular to a kind of and the gas cleaning device gasifying stalk matched with devices.
Background technology
Its complex structure of existing gas cleaning device, manufacturing cost costliness, equipment operation complexity.As: adopt the static decoking, the oxygen level during its operation requires high and wayward, the gas tar oil content height, maintenance cycle is short, and the working cost height is wayward.
The utility model content
The purpose of this utility model is to provide a kind of less investment, maintenance easy to operate, working cost is low, the dedusting decoking is effective, the gas cleaning device of the tar content low (<national standard 70%) after purifying.
The purpose of this utility model is achieved by the following technical programs:
A kind of gas cleaning device that the utility model provides, comprise inlet pipe, water block condensation storehouse, cyclonic separation storehouse, gas-water separation storehouse, coarse filtration storehouse, smart filtering cabin and escape pipe, more than each integral part in turn by pipe connection, wherein combustion gas is earlier carried out condensation again through water seal face in the water block condensation storehouse.Straw fuel gas is operation under positive pressure in the utility model refining plant, and combustion gas enters the water seal face that at first passes water block condensation storehouse from inlet pipe, and the effect of water seal is that combustion gas is washed and anti-non-return string, and the combustion gas after the washing from bottom to top enters the condensation of condensation storehouse.Condensed combustion gas enters the cyclonic separation storehouse and carries out entering the gas-water separation storehouse through pipeline and removing part moisture content and tar after water, gas, dirt separates.Entering the coarse filtration storehouse then further absorbs the moisture content in the combustion gas, tar etc. and filtration.Enter fine filter storehouse afterwards, pass meticulous filtrate and discharge clean inflammable gas, clean inflammable gas is discharged by escape pipe and is delivered to gas-holder or user.
Combustion gas can be isolated sewage and dirt through the processing in above-mentioned each step, for ease of inspection and maintenance, the corresponding inlet pipe in body of the present utility model top, water block condensation storehouse, cyclonic separation storehouse, gas-water separation storehouse and smart filtering cabin are respectively equipped with inspection window, and the side is respectively equipped with sewage draining exit; Corresponding coarse filtration storehouse, described body top is provided with feed port, and the side is provided with discharge port and sewage draining exit, is convenient to change coarse media.
The utlity model has following beneficial effect: less investment, maintenance easy to operate, working cost is low, the dedusting decoking is effective, the tar content low (<national standard 70%) after purifying.
Description of drawings
Below in conjunction with embodiment and accompanying drawing the utility model is described in further detail:
Fig. 1 is the front view of the utility model embodiment;
Fig. 2 is the vertical view of Fig. 1;
Fig. 3 is the A-A view of Fig. 1.
Embodiment
Fig. 1~Figure 3 shows that embodiment of the present utility model comprises inlet pipe 1, water block condensation storehouse 2, cyclonic separation storehouse 3, gas-water separation storehouse 4, coarse filtration storehouse 5, smart filtering cabin 6 and escape pipe 8, more than each integral part in turn by pipe connection.Wherein combustion gas is carried out condensation again through water seal face earlier in the water block condensation storehouse 2, and water seal face is located at the 300mm place that exceeds outlet at bottom.
The corresponding inlet pipe 1 in present embodiment gas cleaning device top, water block condensation storehouse 2, cyclonic separation storehouse 3, gas-water separation storehouse 4 and smart filtering cabin 6 are respectively equipped with inspection window 18,21,31,41 and 61, the corresponding inlet pipe 1 in side is provided with inspection window 9 and 15, to check in the air inlet tube wall and the charred ashes situation bottom the inlet mouth, be convenient to maintenance and mediation; The corresponding inlet pipe 1 in side, cyclonic separation storehouse 3, gas-water separation storehouse 4, coarse filtration storehouse 5 and smart filtering cabin 6 also are respectively equipped with sewage draining exit 13,12,10,11 and 17.Corresponding coarse filtration storehouse, device top 5 is provided with feed port 51, and the side is provided with discharge port 7, is convenient to change coarse media.The device lower end also is provided with sewage draining exit 14 and 16.
During the device operation, opening lift pump earlier adds in water block condensation storehouse about water height 300mm from the air inlet mouth of pipe, restart off-gas pump, this moment, refining plant was an operation under positive pressure, straw fuel gas is entered from top to bottom by inlet pipe 1 and flows, pass bottom 300mm water seal face gas and upwards flow, the height of bottom water level is by sewage draining exit 13 controls; After the cooling of combustion gas through condensation storehouse 2, discharge from air outlet, top, condensation storehouse, along pipeline be folded down and by under enter cyclonic separation storehouse 3 and upwards flow, discharge from sewage draining exit 12 through the sewage that cyclonic separation goes out, gas flows to 4 bottoms, air water separator storehouse by top, and from top to bottom flows isolated sewage by sewage draining exit 11 discharges; Air-flow enters coarse filtration storehouse 5 along pipe and flows from bottom to top, and the water in the combustion gas, tar are filtered, and sewage is discharged by sewage draining exit 10, opens discharge port 7, and the filtrate every three months is changed once; Combustion gas flow to fine filter storehouse 6 from top to bottom along tube side, and after combustion gas was passed through fine filtering from the bottom to top, sewage or impurity were discharged from sewage draining exit 17, and each year cleaning of fine filtering material once.Gas-holder or user are discharged and delivered to clean combustion gas by fine filter storehouse 6 upper outlets through escape pipe 8.
Inspection window is to check once each month; when operation device, sewage draining exit blowdown in per 20 minutes once, before device is stopped transport; must open sewage draining exit 10,11,12,17 discharging about 5 minutes earlier, open sewage draining exit 14,16 after the shutdown again the water in the refining plant is all drained.The coarse filtration material was changed once in per 3 months, and every replacing is once fed in raw material about high 1200mm from feed port 51.The once meticulous filtrate of every three months inspection, each year cleaning of meticulous filtrate once.

Claims (2)

1, a kind of gas cleaning device, it is characterized in that: comprise inlet pipe, water block condensation storehouse, cyclonic separation storehouse, gas-water separation storehouse, coarse filtration storehouse, smart filtering cabin and escape pipe, more than each integral part in turn by pipe connection, wherein combustion gas earlier enters the condensation storehouse again through water seal face in the water block condensation storehouse.
2, gas cleaning device according to claim 1 is characterized in that: the corresponding inlet pipe in the top of body, water block condensation storehouse, cyclonic separation storehouse, gas-water separation storehouse and smart filtering cabin are respectively equipped with inspection window, and the side is respectively equipped with sewage draining exit; Corresponding coarse filtration storehouse, the top of body is provided with feed port, and the side is provided with discharge port and sewage draining exit.
CN 200420070805 2004-06-24 2004-06-24 Gas burning purifier Expired - Fee Related CN2723459Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200420070805 CN2723459Y (en) 2004-06-24 2004-06-24 Gas burning purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200420070805 CN2723459Y (en) 2004-06-24 2004-06-24 Gas burning purifier

Publications (1)

Publication Number Publication Date
CN2723459Y true CN2723459Y (en) 2005-09-07

Family

ID=35037089

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200420070805 Expired - Fee Related CN2723459Y (en) 2004-06-24 2004-06-24 Gas burning purifier

Country Status (1)

Country Link
CN (1) CN2723459Y (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103836855A (en) * 2012-11-22 2014-06-04 美的集团股份有限公司 Container with contamination discharge function
CN104927884A (en) * 2015-05-26 2015-09-23 张文虎 Apparatus for producing combustible gas by catalytically pyrolyzing refuse and method thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103836855A (en) * 2012-11-22 2014-06-04 美的集团股份有限公司 Container with contamination discharge function
CN104927884A (en) * 2015-05-26 2015-09-23 张文虎 Apparatus for producing combustible gas by catalytically pyrolyzing refuse and method thereof

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20050907

Termination date: 20110624