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CN105384206A - Defoaming method of coal chemical-industrial wastewater - Google Patents

Defoaming method of coal chemical-industrial wastewater Download PDF

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Publication number
CN105384206A
CN105384206A CN201510759808.2A CN201510759808A CN105384206A CN 105384206 A CN105384206 A CN 105384206A CN 201510759808 A CN201510759808 A CN 201510759808A CN 105384206 A CN105384206 A CN 105384206A
Authority
CN
China
Prior art keywords
water
froth breaking
shower nozzle
type filter
coal chemical
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
CN201510759808.2A
Other languages
Chinese (zh)
Inventor
黄开东
李强
王先锋
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.)
Magnificent Environment Public Works In East Anhui LLC
East China Engineering Science and Technology Co Ltd
Original Assignee
Magnificent Environment Public Works In East Anhui LLC
East China Engineering Science and Technology 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 Magnificent Environment Public Works In East Anhui LLC, East China Engineering Science and Technology Co Ltd filed Critical Magnificent Environment Public Works In East Anhui LLC
Priority to CN201510759808.2A priority Critical patent/CN105384206A/en
Publication of CN105384206A publication Critical patent/CN105384206A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/20Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/34Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/12Prevention of foaming

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Nozzles (AREA)

Abstract

The invention discloses a defoaming method of coal chemical-industrial wastewater. According to the defoaming method, defoaming water is extracted from a secondary sedimentation tank of a biochemical pool by virtue of a defoaming water pressure pump, is filtered through a Y-shaped filter and is conveyed to each defoaming nozzle, and atomized defoaming water is sprayed into the biochemical pool by each defoaming nozzle, thereby realizing the defoaming in the biochemical pool; the defoaming capacity is relatively high, and fresh water does not need to be collected, so that the water resource is greatly saved, and the integral water yield load is not increased; meanwhile, by forming an access hole, the daily maintenance is facilitated.

Description

A kind of coal chemical industrial waste water debubbling method
Technical field
The present invention relates to Coal Chemical Industry phenolic wastewater aerobic treatment method field, specifically a kind of coal chemical industrial waste water debubbling method.
Background technology
In Coal Chemical Industry phenol ammonia waste water or Treatment of Coking Effluent project, due to containing a large amount of phenolic wastewater, it can produce a large amount of foams when aerobic biochemical, froth breaking generally adopts defoamer or water smoke froth breaking, adopt defoamer cost higher, can secondary pollution be brought, increase sewage treatment load.Adopt water smoke froth breaking then can consume large water gaging, adopt fresh water can cause consumption great lot of water resources, the water of biochemical treatment system inside is adopted to carry out froth breaking, great lot of water resources can be saved, water froth breaking is then that water is sprayed into water smoke, destroy by the surface tension of band pressure water smoke to foam, thus obtain froth breaking object.
The water of biochemical treatment system, is still having a large amount of suspended substance, mud and some other impurity after settling tank precipitation, for can blocking pipe and shower nozzle during froth breaking.In northern cold cold wind sand ground territory, biochemistry pool often needs to add a cover, and cannot overhaul when shower nozzle blocks, and brings much run difficulty to engineering.
summary of the inventionthe object of this invention is to provide a kind of coal chemical industrial waste water debubbling method, to solve prior art biochemistry pool froth breaking Problems existing.
In order to achieve the above object, the technical solution adopted in the present invention is:
A kind of coal chemical industrial waste water debubbling method, it is characterized in that: using the secondary sedimentation basins water outlet of biochemistry pool as froth breaking water, in biochemistry pool top glass steel cage, both sides arrange multiple froth breaking shower nozzle respectively, both sides froth breaking shower nozzle equal altitudes and respectively with 45 ° of inclination angles towards in biochemistry pool, adopt froth breaking water force (forcing) pump, y-type filter, froth breaking water force (forcing) pump water-in is communicated with the water outlet of secondary sedimentation basins, the water outlet of froth breaking water force (forcing) pump is communicated with y-type filter water-in, is communicated with respectively by each froth breaking shower nozzle each via trip valve with the water outlet of y-type filter; Draw froth breaking water by froth breaking water force (forcing) pump from the secondary sedimentation basins of biochemistry pool, and in froth breaking water is sent into each froth breaking shower nozzle after y-type filter filters, in biochemistry pool, spray vaporific froth breaking water by each froth breaking shower nozzle, realize froth breaking in biochemistry pool.
Described a kind of coal chemical industrial waste water debubbling method, is characterized in that: y-type filter filters the medium-and-large-sized floating matter of froth breaking water, alleviates the blocking to pipeline and shower nozzle, is regularly cleared up by the impurity of y-type filter, avoid y-type filter to block.
Described a kind of coal chemical industrial waste water debubbling method, is characterized in that: the trip valve of regularly closed portion froth breaking shower nozzle connection, makes the water yield of residue froth breaking shower nozzle increase, and pressure raises simultaneously, to wash away remaining froth breaking shower nozzle, alleviates blocking.
Described a kind of coal chemical industrial waste water debubbling method, it is characterized in that: in glass fibre reinforced plastic cover, the position of each froth breaking shower nozzle corresponding arranges the access hole that diameter is not less than 300mm respectively, access hole place adopts glass fiber reinforced plastic flange lid to cover, and easy access, avoids foam excessive from access hole simultaneously.
Described a kind of coal chemical industrial waste water debubbling method, is characterized in that: froth breaking shower nozzle adopts conical hollow spiral spray nozzle, because shower nozzle is hollow, then alleviates blocked, and cone-type spiral is the prerequisite forming water smoke simultaneously.
The present invention using water outlet in biochemistry pool secondary sedimentation basins as froth breaking water, and as biochemistry pool froth breaking water after being filtered by y-type filter, has good defoaming capacity, and need not adopt fresh water, has greatly saved water resources, can not increase overall water yield load.Be that maintenance repair is provided convenience by arranging access hole simultaneously.
Accompanying drawing explanation
Fig. 1 is principle of the invention piping system figure.
Fig. 2 is froth breaking nozzle layout of sprinkler floor map in the present invention.
Fig. 3 is froth breaking nozzle layout of sprinkler orthogonal view in the present invention.
Embodiment
Shown in Fig. 1-Fig. 3, a kind of coal chemical industrial waste water debubbling method, using the secondary sedimentation basins water outlet 1 of biochemistry pool as froth breaking water, in biochemistry pool top glass steel cage 2, both sides arrange multiple froth breaking shower nozzle 3 respectively, both sides froth breaking shower nozzle 3 equal altitudes and respectively with 45 ° of inclination angles towards in biochemistry pool, adopt froth breaking water force (forcing) pump 4, y-type filter 5, froth breaking water force (forcing) pump 4 water-in is communicated with the water outlet of secondary sedimentation basins, the water outlet of froth breaking water force (forcing) pump 4 is communicated with y-type filter 5 water-in, each froth breaking shower nozzle 3 is communicated with each via the water outlet of trip valve 6 with y-type filter 5 respectively, froth breaking water is drawn from the secondary sedimentation basins of biochemistry pool by froth breaking water force (forcing) pump 4, and in froth breaking water is sent into each froth breaking shower nozzle 3 after y-type filter 4 filters, in biochemistry pool, spray vaporific froth breaking water by each froth breaking shower nozzle 3, realize froth breaking in biochemistry pool.
Y-type filter 4 filters the medium-and-large-sized floating matter of froth breaking water, alleviates the blocking to pipeline and shower nozzle, is regularly cleared up by the impurity of y-type filter, avoid y-type filter to block.
The trip valve 6 that regular closed portion froth breaking shower nozzle connects, makes the water yield of residue froth breaking shower nozzle increase, and pressure raises simultaneously, to wash away remaining froth breaking shower nozzle, alleviates blocking.
In glass fibre reinforced plastic cover 2, the position of each froth breaking shower nozzle 3 corresponding arranges the access hole 7 that diameter is not less than 300mm respectively, and access hole 7 place adopts glass fiber reinforced plastic flange lid to cover, and easy access, avoids foam excessive from access hole simultaneously.
Froth breaking shower nozzle 3 adopts conical hollow spiral spray nozzle, because shower nozzle is hollow, then alleviates blocked, and cone-type spiral is the prerequisite forming water smoke simultaneously.

Claims (5)

1. a coal chemical industrial waste water debubbling method, it is characterized in that: using the secondary sedimentation basins water outlet of biochemistry pool as froth breaking water, in biochemistry pool top glass steel cage, both sides arrange multiple froth breaking shower nozzle respectively, both sides froth breaking shower nozzle equal altitudes and respectively with 45 ° of inclination angles towards in biochemistry pool, adopt froth breaking water force (forcing) pump, y-type filter, froth breaking water force (forcing) pump water-in is communicated with the water outlet of secondary sedimentation basins, the water outlet of froth breaking water force (forcing) pump is communicated with y-type filter water-in, is communicated with respectively by each froth breaking shower nozzle each via trip valve with the water outlet of y-type filter; Draw froth breaking water by froth breaking water force (forcing) pump from the secondary sedimentation basins of biochemistry pool, and in froth breaking water is sent into each froth breaking shower nozzle after y-type filter filters, in biochemistry pool, spray vaporific froth breaking water by each froth breaking shower nozzle, realize froth breaking in biochemistry pool.
2. a kind of coal chemical industrial waste water debubbling method according to claim 1, it is characterized in that: y-type filter filters the medium-and-large-sized floating matter of froth breaking water, alleviate the blocking to pipeline and shower nozzle, regularly the impurity of y-type filter is cleared up, avoid y-type filter to block.
3. a kind of coal chemical industrial waste water debubbling method according to claim 1, is characterized in that: the trip valve of regularly closed portion froth breaking shower nozzle connection, makes the water yield of residue froth breaking shower nozzle increase, and pressure raises simultaneously, to wash away remaining froth breaking shower nozzle, alleviates blocking.
4. a kind of coal chemical industrial waste water debubbling method according to claim 1, it is characterized in that: in glass fibre reinforced plastic cover, the position of each froth breaking shower nozzle corresponding arranges the access hole that diameter is not less than 300mm respectively, access hole place adopts glass fiber reinforced plastic flange lid to cover, easy access, avoids foam excessive from access hole simultaneously.
5. a kind of coal chemical industrial waste water debubbling method according to claim 1, is characterized in that: froth breaking shower nozzle adopts conical hollow spiral spray nozzle, because shower nozzle is hollow, then alleviates blocked, and cone-type spiral is the prerequisite forming water smoke simultaneously.
CN201510759808.2A 2015-11-05 2015-11-05 Defoaming method of coal chemical-industrial wastewater Pending CN105384206A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510759808.2A CN105384206A (en) 2015-11-05 2015-11-05 Defoaming method of coal chemical-industrial wastewater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510759808.2A CN105384206A (en) 2015-11-05 2015-11-05 Defoaming method of coal chemical-industrial wastewater

Publications (1)

Publication Number Publication Date
CN105384206A true CN105384206A (en) 2016-03-09

Family

ID=55417048

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510759808.2A Pending CN105384206A (en) 2015-11-05 2015-11-05 Defoaming method of coal chemical-industrial wastewater

Country Status (1)

Country Link
CN (1) CN105384206A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112759189A (en) * 2020-12-29 2021-05-07 华夏碧水环保科技有限公司北京分公司 A fire fighting equipment for sewage biochemical treatment
CN114763274A (en) * 2021-01-14 2022-07-19 中国石油化工股份有限公司 Defoaming device and defoaming method for biological fluidized bed reactor

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101838044A (en) * 2010-03-17 2010-09-22 哈尔滨工业大学 Method and device for eliminating foam Lurgi furnance coal gas wastewater treatment process
CN102276057A (en) * 2011-07-07 2011-12-14 江苏高朗环境技术有限公司 Accurate aeration and combined defoaming technological scheme for waste leachate treatment
WO2012084480A1 (en) * 2010-12-20 2012-06-28 Siemens Vai Metals Technologies Gmbh Method and apparatus for treating process water
CN202492407U (en) * 2012-02-23 2012-10-17 上海申兰环保有限公司 Foam removing device
KR20150012761A (en) * 2013-07-26 2015-02-04 주식회사 에이에프티코리아 Wastewater treatment system

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101838044A (en) * 2010-03-17 2010-09-22 哈尔滨工业大学 Method and device for eliminating foam Lurgi furnance coal gas wastewater treatment process
WO2012084480A1 (en) * 2010-12-20 2012-06-28 Siemens Vai Metals Technologies Gmbh Method and apparatus for treating process water
CN102276057A (en) * 2011-07-07 2011-12-14 江苏高朗环境技术有限公司 Accurate aeration and combined defoaming technological scheme for waste leachate treatment
CN202492407U (en) * 2012-02-23 2012-10-17 上海申兰环保有限公司 Foam removing device
KR20150012761A (en) * 2013-07-26 2015-02-04 주식회사 에이에프티코리아 Wastewater treatment system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112759189A (en) * 2020-12-29 2021-05-07 华夏碧水环保科技有限公司北京分公司 A fire fighting equipment for sewage biochemical treatment
CN114763274A (en) * 2021-01-14 2022-07-19 中国石油化工股份有限公司 Defoaming device and defoaming method for biological fluidized bed reactor

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Application publication date: 20160309