CN101147891B - High-performance charge pre-agglomerated electric tar corrector - Google Patents

High-performance charge pre-agglomerated electric tar corrector Download PDF

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Publication number
CN101147891B
CN101147891B CN2007101195469A CN200710119546A CN101147891B CN 101147891 B CN101147891 B CN 101147891B CN 2007101195469 A CN2007101195469 A CN 2007101195469A CN 200710119546 A CN200710119546 A CN 200710119546A CN 101147891 B CN101147891 B CN 101147891B
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China
Prior art keywords
tar
gas
charge
district
agglomerated
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Expired - Fee Related
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CN2007101195469A
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Chinese (zh)
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CN101147891A (en
Inventor
夏德宏
卢娇
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University of Science and Technology Beijing USTB
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University of Science and Technology Beijing USTB
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Priority to CN2007101195469A priority Critical patent/CN101147891B/en
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Publication of CN101147891B publication Critical patent/CN101147891B/en
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Abstract

The present invention relates to a high-effective charged preagglomeration type electric tar-trapping device, belonging to the field of environmental protection engineering technology, and relates to a gas purifying device in the coal conversion process. It is characterized by that it adopts a charged preaggomeration method to make the microfine tar atomized drops being in the thermal dirty gas or raw cake oven gas be previously agglomerated into large atomized drops. Said device includes external power supply, dirty (raw coke oven) gas inlet, precharging stage, mixing stage, main tar-trapping zone, clean gas outlet, valves and tar outlet.

Description

A kind of high-performance charge pre-agglomerated electric tar corrector
Technical field:
The invention belongs to field of environmental engineering, relate to the gas cleaning device in a kind of coal conversion processes, the charged pre-method of agglomeration of particularly a kind of employing makes the fine tar droplet in hot dirty gas or the raw coke oven gas be agglomerated into big droplet in advance.
Technical background:
The general structure that adopts single or multiple tar to capture the district of traditional electrical tar precipitator.But this traditional structure is directly introduced tar capture district with hot dirty gas or raw coke oven gas, fine tar droplet is not carried out preliminary treatment, causes it can not capture fine tar droplet effectively, and is not high to the overall purification efficiency of hot dirty gas and raw coke oven gas; In addition, the fine tar droplet that is mingled with in the coal gas also can cause follow-up line clogging.
Summary of the invention
The objective of the invention is directly hot dirty gas or raw coke oven gas to be introduced tar capture district in order to solve traditional electrical tar precipitator, can not capture effectively fine tar droplet, the fine tar droplet that the overall purification efficiency of hot dirty gas and raw coke oven gas is mingled with in the not high and coal gas also can cause the problem of follow-up line clogging.
A kind of high-performance charge pre-agglomerated electric tar corrector, it is characterized in that having increased pre-reunion district, the pre-district of reuniting is divided into pre-charged section and mixer again, the pre-charged section layout 2-8 root metal tube that goes in ring, every metal tube central authorities add a thin corona wire, and adjacent corona wire connects the positive pole and the negative pole of power supply respectively.After the energising, tar fog drops in and is forced to lotus in the electric field with positive charge or negative electrical charge, and adjacent corona wire is connected to the positive pole of power supply and negative pole and helps tar fog with the heteropolarity electric charge and drop in mixer and reunite in advance better.Mixer is one section blank pipe, and the tar fog of heteropolarity drops in this section interval and attracted each other by the effect of Coulomb force and pre-reunion takes place, and has realized that the tar droplet from the differentiation of small particle diameter to big particle diameter, helps the capture of fine tar droplet.Tar droplet positive and negative charge after taking place to reunite is in advance cancelled out each other, show electroneutral, catch in the tar district chargedly again, and under the effect of electric field force, move to receiving electrode main, be deposited at last on the receiving electrode, electrical tar precipitator has obtained promoting significantly to the arresting efficiency of fine tar droplet.
The basic principle of charged pre-reunion is that waste (dirty) coal gas is introduced the different electric field of polarity, makes wherein part tar droplet positively charged, and another part tar droplet is electronegative.After waste (dirty) coal gas confluxed, the tar fog of band heteropolarity electric charge dropped in and attracts each other under the effect of electric field force and reunite, and realizes that finally fine tar droplet is agglomerated into the purpose of big droplet in advance.
The present invention compares with traditional electrical tar precipitator, and have following two big outstanding advantages: (1) is to the arresting efficiency height of fine tar droplet.(2) can capture the ultra-fine tar droplet that traditional electrical tar precipitator can not trap effectively.
Description of drawings
Fig. 1 is the structure diagram of high-performance charge pre-agglomerated electric tar corrector.
The 1-external power supply; 2-dirty (famine) gas entry; Pre-charged section of 3-; The 4-mixer; 5-master catches the tar district; The outlet of 6-clean gas; 7-valve 1; 8-valve 2; The outlet of 9-tar
The specific embodiment
1. 1 kinds of high-performance charge pre-agglomerated electric tar correctors of embodiment comprise the 1-external power supply; 2-dirty (famine) gas entry; Pre-charged section of 3-; The 4-mixer; 5-master catches the tar district; The outlet of 6-clean gas; 7-valve 1; 8-valve 2; The outlet of 9-tar.Pre-charged section 2 metal tubes of layout that go in ring, every metal tube central authorities add a thin corona wire, and adjacent corona wire connects the positive pole and the negative pole of power supply respectively.After the energising, tar fog drops in and is forced to lotus in the electric field with positive charge or negative electrical charge, and adjacent corona wire is connected to the positive pole of power supply and negative pole and helps tar fog with the heteropolarity electric charge and drop in mixer and reunite in advance better.
Embodiment 2. pre-charged section 4 metal tubes of layout that go in ring, every metal tube central authorities add a thin corona wire, and adjacent corona wire connects the positive pole and the negative pole of power supply respectively.After the energising, tar fog drops in and is forced to lotus in the electric field with positive charge or negative electrical charge.
Embodiment 3. pre-charged section 8 metal tubes of layout that go in ring, every metal tube central authorities add a thin corona wire, and adjacent corona wire connects the positive pole and the negative pole of power supply respectively.After the energising, tar fog drops in and is forced to lotus in the electric field with positive charge or negative electrical charge.

Claims (1)

1. high-performance charge pre-agglomerated electric tar corrector, it is characterized in that having increased pre-reunion district, the pre-district of reuniting is divided into pre-charged section and mixer again, the pre-charged section layout 2-8 root metal tube that goes in ring, every metal tube central authorities add a thin corona wire, and adjacent corona wire connects the positive pole and the negative pole of power supply respectively; After the energising, tar fog drops in and is forced to lotus in the electric field with positive charge or negative electrical charge; Mixer is one section blank pipe, and the tar fog of heteropolarity drops in this section interval and attracted each other by the effect of Coulomb force and pre-reunion takes place, and has realized that the tar droplet is from the differentiation of small particle diameter to big particle diameter; The tar droplet positive and negative charge that takes place after pre-the reunion is cancelled out each other, and shows electroneutral, catches in the tar district chargedly again main, and moves to receiving electrode under the effect of electric field force, is deposited on the receiving electrode at last.
CN2007101195469A 2007-07-26 2007-07-26 High-performance charge pre-agglomerated electric tar corrector Expired - Fee Related CN101147891B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2007101195469A CN101147891B (en) 2007-07-26 2007-07-26 High-performance charge pre-agglomerated electric tar corrector

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2007101195469A CN101147891B (en) 2007-07-26 2007-07-26 High-performance charge pre-agglomerated electric tar corrector

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CN101147891A CN101147891A (en) 2008-03-26
CN101147891B true CN101147891B (en) 2010-09-15

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Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106152801B (en) * 2015-04-23 2019-03-01 沈阳铝镁科技有限公司 A kind of baking flue gas tar controlling device and method
CN111822146A (en) * 2019-04-15 2020-10-27 中国科学院过程工程研究所 Pre-charging electric appliance
CN114146819B (en) * 2021-12-02 2022-08-30 襄阳九鼎昊天环保设备有限公司 Electric tar precipitator with corona electrode anti-swing structure

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4145191A (en) * 1977-04-13 1979-03-20 Kunchal S Kumar Gas stream cleaning system and method
US4247308A (en) * 1979-06-11 1981-01-27 Air Pollution Technology, Inc. Preformed-spray scrubber
US4443234A (en) * 1981-04-03 1984-04-17 Flakt Aktiebolag Device at a dust filter
CN2042378U (en) * 1988-09-28 1989-08-09 汪波 Electrostatic tar collecting apparatus
CN1142784A (en) * 1994-01-03 1997-02-12 孟山都公司 Apparatus and method for controlling pollution

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4145191A (en) * 1977-04-13 1979-03-20 Kunchal S Kumar Gas stream cleaning system and method
US4247308A (en) * 1979-06-11 1981-01-27 Air Pollution Technology, Inc. Preformed-spray scrubber
US4443234A (en) * 1981-04-03 1984-04-17 Flakt Aktiebolag Device at a dust filter
CN2042378U (en) * 1988-09-28 1989-08-09 汪波 Electrostatic tar collecting apparatus
CN1142784A (en) * 1994-01-03 1997-02-12 孟山都公司 Apparatus and method for controlling pollution

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GR01 Patent grant
EE01 Entry into force of recordation of patent licensing contract

Assignee: Danyang Jiangnan Industrial Furnace Co., Ltd.

Assignor: University of Science and Technology Beijing

Contract record no.: 2012320000345

Denomination of invention: High-performance charge pre-agglomerated electric tar corrector

Granted publication date: 20100915

License type: Exclusive License

Open date: 20080326

Record date: 20120329

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Granted publication date: 20100915

Termination date: 20130726