CN105435566A - Dust removing device for white carbon black production - Google Patents

Dust removing device for white carbon black production Download PDF

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Publication number
CN105435566A
CN105435566A CN201510841893.7A CN201510841893A CN105435566A CN 105435566 A CN105435566 A CN 105435566A CN 201510841893 A CN201510841893 A CN 201510841893A CN 105435566 A CN105435566 A CN 105435566A
Authority
CN
China
Prior art keywords
white carbon
tower body
storage tank
carbon black
dust removing
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
CN201510841893.7A
Other languages
Chinese (zh)
Inventor
肖建军
许道立
刘改正
张国峰
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.)
LUOYANG LVREN ENVIRONMENTAL PROTECTION EQUIPMENT Co Ltd
Original Assignee
LUOYANG LVREN ENVIRONMENTAL PROTECTION 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 LUOYANG LVREN ENVIRONMENTAL PROTECTION EQUIPMENT Co Ltd filed Critical LUOYANG LVREN ENVIRONMENTAL PROTECTION EQUIPMENT Co Ltd
Priority to CN201510841893.7A priority Critical patent/CN105435566A/en
Publication of CN105435566A publication Critical patent/CN105435566A/en
Pending legal-status Critical Current

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Abstract

The invention provides a dust removing device for white carbon black production. The dust removing device comprises a dust removing tower and a temporary liquid storage tank, wherein the dust removing tower comprises a tower body and a water inlet pipe coiled in the tower body, a gas inlet and a liquid outlet are formed in the bottom of the tower body, spray nozzles are arranged on the water inlet pipe, the liquid outlet is communicated with the temporary liquid storage tank, overflow weirs are arranged in the temporary liquid storage tank, and the temporary liquid storage tank is connected with an exhaust fan through a cyclone dust collector. The dust removing device for white carbon black production has the advantages of scientific design, high practicability, high production efficiency, reliable dust removing quality and good dust removing effect.

Description

White carbon black production dust arrester
Technical field
The present invention relates to a kind of cleaner, specifically, relate to a kind of white carbon black production dust arrester.
Background technology
Vapor phase method is produced in the process of white carbon, a large amount of tail gas can be produced, these tail gas have to pass through process can arrive emission request, simultaneously owing to containing a large amount of silica particles in tail gas, if do not process these particles, be bound to occluding device, causes production to proceed, how to remove the white carbon in tail gas and ensure that pipeline does not block, people's problem demanding prompt solution.
In order to solve above Problems existing, people are seeking a kind of desirable technical solution always.
Summary of the invention
The object of the invention is for the deficiencies in the prior art, thus a kind of design science is provided, practical, production efficiency is high, the white carbon black production dust arrester of dedusting reliable in quality and good dedusting effect.
To achieve these goals, the technical solution adopted in the present invention is: a kind of white carbon black production dust arrester, it comprises gas wash tower and liquid temporary storage tank, described gas wash tower comprises tower body and coils the inlet channel being located at described tower body inside, air inlet and liquid outlet is respectively arranged with bottom described tower body, described inlet channel is provided with nozzle, described liquid outlet is communicated with described liquid temporary storage tank, be provided with downflow weir in described liquid temporary storage tank, described liquid temporary storage tank is connected with air exhauster by cyclone dust collectors.
Based on above-mentioned, described air inlet is arranged on the sidewall of described tower body, and described air inlet place is provided with air blast.
Based on above-mentioned, described inlet channel stretches out described tower body and arranges and be connected with force (forcing) pump.
Based on above-mentioned, in described tower body, be staggeredly equipped with dividing plate, described dividing plate is provided with spout hole.
Based on above-mentioned, described nozzle is evenly distributed on described inlet channel.
Hinge structure of the present invention has outstanding substantive distinguishing features and significant progress, specifically, the present invention utilizes described gas wash tower to absorb the white carbon in tail gas, liquid after absorption enters described liquid temporary storage tank, and precipitated by described downflow weir, the silica particles removed in tail gas with this prevents the blocking of equipment; It has design science, practical, production efficiency is high, the advantage of dedusting reliable in quality and good dedusting effect.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Detailed description of the invention
Below by detailed description of the invention, technical scheme of the present invention is described in further detail.
As shown in Figure 1, a kind of white carbon black production dust arrester, it comprises gas wash tower and liquid temporary storage tank, is reclaimed by the silica particles in white carbon black production tail gas with this.Described gas wash tower comprises tower body 1 and coils the inlet channel 2 being located at described tower body 1 inside, adopts inlet channel dish to establish structure increase the contact area of tail gas and water and ensure that the white carbon in tail gas is thoroughly water-soluble time of contact; Be respectively arranged with air inlet 11 and liquid outlet 12 bottom described tower body 1, tail gas enters described tower body 1 through described air inlet 11 and is fully dissolved by water; Described inlet channel 11 is provided with nozzle, guarantees that silica particles dissolves fully; Described liquid outlet 12 is communicated with described liquid temporary storage tank 3, is provided with downflow weir 31 in described liquid temporary storage tank 3, utilizes described liquid temporary storage tank 3 liquid towards to carry out sedimentation and filtration, makes white carbon be deposited at the bottom of the tank of described liquid temporary storage tank 3 by described downflow weir 31; Described liquid temporary storage tank 3 is connected with air exhauster 5 by cyclone dust collectors 4, utilizes described cyclone dust collectors 4 to filter the gas after washing and is undertaken by described air exhauster 5 extracting ensureing the thorough of dedusting.
In order to ensure dedusting quality, described air inlet 11 is arranged on the sidewall of described tower body 1, and described air inlet 11 place is provided with air blast, utilizes air blast tail gas to be delivered into described tower body 1, guarantees reaction thoroughly fully.Clean-up port is offered, with the white carbon after this scavenger precipitation at the bottom of the tank of described liquid temporary storage tank 3.
In order to ensure the completeness of washing and the abundant of water inlet, described inlet channel 2 stretches out described tower body 1 and arranges and be connected with force (forcing) pump, utilizes the regulation and control of force (forcing) pump water feeding pressure.
In order to ensure that tail gas and water fully react, being staggeredly equipped with dividing plate in described tower body 1, described dividing plate is provided with spout hole, ensureing the completeness of dedusting the time of contact increasing water and tail gas with this.Meanwhile, described nozzle is evenly distributed on described inlet channel 2, ensures the completeness of washing with this.
Finally should be noted that: above embodiment is only in order to illustrate that technical scheme of the present invention is not intended to limit; Although with reference to preferred embodiment to invention has been detailed description, those of ordinary skill in the field are to be understood that: still can modify to the specific embodiment of the present invention or carry out equivalent replacement to portion of techniques feature; And not departing from the spirit of technical solution of the present invention, it all should be encompassed in the middle of the technical scheme scope of request of the present invention protection.

Claims (5)

1. a white carbon black production dust arrester, it is characterized in that: it comprises gas wash tower and liquid temporary storage tank, described gas wash tower comprises tower body and coils the inlet channel being located at described tower body inside, air inlet and liquid outlet is respectively arranged with bottom described tower body, described inlet channel is provided with nozzle, described liquid outlet is communicated with described liquid temporary storage tank, is provided with downflow weir in described liquid temporary storage tank, and described liquid temporary storage tank is connected with air exhauster by cyclone dust collectors.
2. white carbon black production dust arrester according to claim 1, is characterized in that: described air inlet is arranged on the sidewall of described tower body, and described air inlet place is provided with air blast.
3. white carbon black production dust arrester according to claim 1 and 2, is characterized in that: described inlet channel stretches out described tower body and arranges and be connected with force (forcing) pump.
4. white carbon black production dust arrester according to claim 3, is characterized in that: be staggeredly equipped with dividing plate in described tower body, described dividing plate is provided with spout hole.
5. white carbon black production dust arrester according to claim 1, is characterized in that: described nozzle is evenly distributed on described inlet channel.
CN201510841893.7A 2015-11-28 2015-11-28 Dust removing device for white carbon black production Pending CN105435566A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510841893.7A CN105435566A (en) 2015-11-28 2015-11-28 Dust removing device for white carbon black production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510841893.7A CN105435566A (en) 2015-11-28 2015-11-28 Dust removing device for white carbon black production

Publications (1)

Publication Number Publication Date
CN105435566A true CN105435566A (en) 2016-03-30

Family

ID=55546466

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510841893.7A Pending CN105435566A (en) 2015-11-28 2015-11-28 Dust removing device for white carbon black production

Country Status (1)

Country Link
CN (1) CN105435566A (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4353845A (en) * 1981-05-04 1982-10-12 Chartrand Joseph A Gas scrubber
CN2458058Y (en) * 2000-12-25 2001-11-07 武兴文 Smoke prevention and dust control device
CN2505710Y (en) * 2001-09-29 2002-08-14 王宪贵 Double-tube cyclone wet flue gas cleaner
CN201329245Y (en) * 2008-11-29 2009-10-21 刘金钊 Tail gas purification device used after carnallite dehydration
CN201470301U (en) * 2009-07-24 2010-05-19 张振锋 High-pressure non-resistance spiral dedusting and desulfurization purifying device
CN201832523U (en) * 2010-10-28 2011-05-18 无锡市前洲西塘锻压有限公司 Circulating water dedusting recoverer

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4353845A (en) * 1981-05-04 1982-10-12 Chartrand Joseph A Gas scrubber
CN2458058Y (en) * 2000-12-25 2001-11-07 武兴文 Smoke prevention and dust control device
CN2505710Y (en) * 2001-09-29 2002-08-14 王宪贵 Double-tube cyclone wet flue gas cleaner
CN201329245Y (en) * 2008-11-29 2009-10-21 刘金钊 Tail gas purification device used after carnallite dehydration
CN201470301U (en) * 2009-07-24 2010-05-19 张振锋 High-pressure non-resistance spiral dedusting and desulfurization purifying device
CN201832523U (en) * 2010-10-28 2011-05-18 无锡市前洲西塘锻压有限公司 Circulating water dedusting recoverer

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Application publication date: 20160330

RJ01 Rejection of invention patent application after publication