CN202849208U - Wastewater treatment system during production of white spirit - Google Patents

Wastewater treatment system during production of white spirit Download PDF

Info

Publication number
CN202849208U
CN202849208U CN 201220519307 CN201220519307U CN202849208U CN 202849208 U CN202849208 U CN 202849208U CN 201220519307 CN201220519307 CN 201220519307 CN 201220519307 U CN201220519307 U CN 201220519307U CN 202849208 U CN202849208 U CN 202849208U
Authority
CN
China
Prior art keywords
wastewater treatment
pool
treatment system
white spirit
utility
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 201220519307
Other languages
Chinese (zh)
Inventor
梁茂林
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.)
Guangxi Hui Tai Environmental Protection Technology Co Ltd
Original Assignee
Guangxi Hui Tai Environmental Protection 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 Guangxi Hui Tai Environmental Protection Technology Co Ltd filed Critical Guangxi Hui Tai Environmental Protection Technology Co Ltd
Priority to CN 201220519307 priority Critical patent/CN202849208U/en
Application granted granted Critical
Publication of CN202849208U publication Critical patent/CN202849208U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

The utility model provides a wastewater treatment system during production of white spirit, which can effectively transform white spirit wastewater to discharge water. The wastewater treatment system comprises a grille, a regulating pool, a circulating tank, a UASB (upflow anaerobic sludge blanket) pool, an intermediate sedimentation pool, a contact oxidation pool and a secondary sedimentation pool which are connected sequentially. The wastewater treatment system during production of white spirit, provided by the utility model, has the advantages of simple structure and high treatment efficiency, and can achieve discharge standards.

Description

A kind of liquor production wastewater treatment system
Technical field
The utility model relates to a kind of Waste Water Treatment, especially a kind of liquor production wastewater treatment system.
Background technology
Liquor factory effluent source mainly contains soaks rice waste water, wash bottle workshop and tinning workshop waste water, ground flushing water, plant area's sanitary sewage etc.Mostly be organic substance in the waste water, contain suspended substance, ethanol, carbohydrate, protein degradation thing and tunning, it is acid that waste water is.
Specific features is as follows: 1. waste water generally is easy to biological degradation, and B/C suits to carry out a biological disposal upon generally more than 0.5; 2. SS concentration is high in the waste water; 3. water yield intermittently discharged, variation water quality is larger; 4. the fluctuation of waste water pH value is larger; 5. waste water is with color.
According to State Standard of the People's Republic of China GB8978-1996, waste water reaches " comprehensive pollution thing emission standard " primary standard after treatment, but existing Waste Water Treatment is difficult to reach above-mentioned requirements.
The utility model content
The purpose of this utility model provides a kind of liquor production wastewater treatment system that can effectively liquor waste water be converted into discharge water.
Realize the liquor production wastewater treatment system of the utility model purpose, comprise the grid, equalizing tank, circulation tank, UASB pond, medium sediment pool, contact-oxidation pool and the second pond that link to each other successively.
Described medium sediment pool, contact-oxidation pool and second pond connect respectively sludge drying bed, and the percolate outlet of described sludge drying bed is connected with equalizing tank.
The beneficial effects of the utility model are as follows: liquor production wastewater treatment of the present utility model system, and simple in structure, processing efficiency is high, can reach emission standard.
Description of drawings
Fig. 1 is the structural representation of liquor production wastewater treatment of the present utility model system.
Embodiment
Embodiment of the present utility model is as follows: as shown in Figure 1, liquor production wastewater treatment of the present utility model system comprises the grid, equalizing tank, circulation tank, UASB pond, medium sediment pool, contact-oxidation pool and the second pond that link to each other successively.
Described medium sediment pool, contact-oxidation pool and second pond connect respectively sludge drying bed, and the percolate outlet of described sludge drying bed is connected with equalizing tank.
The working process of liquor production wastewater treatment of the present utility model system is as follows: liquor Workshop Production waste water behind pipe influx through grid, the larger solid substance of scrubbing and twister, entering subsequently equalizing tank stores, the waste water that waste water promotes through lift pump fully mixes in circulation tank with the anaerobism mixed solution of medium sediment pool backflow and dilutes, and be evenly distributed in the UASB Sludge Bed, stirring by water inlet and biogas, water inlet is fully contacted with anaerobic mud bed mud, greatly improved the clearance of the organic pollutant in the water, most pollutent is removed (the COD clearance reaches more than 85%) in this link, the anaerobism final product is biogas, synthetic cell, the a small amount of scum silica frost of water etc., effect by triphase separator, mud in the UASB pond, water, gas separates, mud is by certainly flowing back to Sludge Bed, biogas leads to water-sealed tank by drainage system to be processed, and water then enters follow-up medium sediment pool; The part anaerobic sludge being continued precipitation in medium sediment pool and utilize pump to promote to be back to circulation tank enters the UASB pond and guarantees sludge concentration, upper liquid enters contact-oxidation pool, a large amount of active sludge in the contact-oxidation pool, utilize under the condition of outside oxygen supply, metabolism and the synthetic acting in conjunction of oxidation through active sludge, further remove the remaining Components of Organic Pollutants in the water, final product is water, synthetic cell, a small amount of residual gas etc., after water outlet is clarified through settling tank, the bottom sludge reflux is to the contact-oxidation pool front end, guarantee the concentration of aerobic treatment bacterial classification, the supernatant liquor discharging.
The sludge disposal that produces in the system, the excess sludge of biological treatment are through the sludge drying bed dehydration and drying, and dewatered sludge outward transport landfill is disposed, and filtrate is back to water collecting basin and continues to process.
Liquor production wastewater treatment advantage of system of the present utility model is as follows: up-flow anaerobic sludge blanket (UASB) is a kind of efficient anaerobic process reactor, its characteristics are that sludge concentration is high, the processing load is high, anti impulsion load is strong, stable, hydraulic detention time is short, and the capital construction cost is low etc.; Contact-oxidation pool is to adopt more aerobic treatment process in the trade effluent, and reason is the shortcoming that this technique has overcome traditional activated sludge process, has denitrogenation dephosphorizing function, strong shock resistance, characteristics that load is high.
Embodiment recited above is described preferred implementation of the present utility model; be not that scope of the present utility model is limited; design under the spiritual prerequisite not breaking away from the utility model; various distortion and improvement that the common engineering technical personnel in this area make technical solutions of the utility model all should fall in the definite protection domain of claims of the present utility model.

Claims (2)

1. a liquor production wastewater treatment system is characterized in that: comprise the grid, equalizing tank, circulation tank, UASB pond, medium sediment pool, contact-oxidation pool and the second pond that link to each other successively.
2. liquor production wastewater treatment according to claim 1 system is characterized in that: described medium sediment pool, contact-oxidation pool and second pond respectively connect sludge drying bed, and the percolate outlet of described sludge drying bed is connected with equalizing tank.
CN 201220519307 2012-09-20 2012-09-20 Wastewater treatment system during production of white spirit Expired - Fee Related CN202849208U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220519307 CN202849208U (en) 2012-09-20 2012-09-20 Wastewater treatment system during production of white spirit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220519307 CN202849208U (en) 2012-09-20 2012-09-20 Wastewater treatment system during production of white spirit

Publications (1)

Publication Number Publication Date
CN202849208U true CN202849208U (en) 2013-04-03

Family

ID=47980428

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220519307 Expired - Fee Related CN202849208U (en) 2012-09-20 2012-09-20 Wastewater treatment system during production of white spirit

Country Status (1)

Country Link
CN (1) CN202849208U (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103508629A (en) * 2013-09-12 2014-01-15 江苏和顺环保股份有限公司 Wastewater treatment system for food industry
CN103739140A (en) * 2013-11-15 2014-04-23 安徽省绿巨人环境技术有限公司 Liquor factory high-concentration organic wastewater treatment technology
CN104478170A (en) * 2014-12-13 2015-04-01 周桂英 Draught beer mill wastewater treatment method and treatment device
CN104496115A (en) * 2014-12-13 2015-04-08 周桂英 Draft beer plant wastewater treatment method and treatment device
CN104529066A (en) * 2014-12-13 2015-04-22 周桂英 Method and device for treating wastewater of breweries

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103508629A (en) * 2013-09-12 2014-01-15 江苏和顺环保股份有限公司 Wastewater treatment system for food industry
CN103739140A (en) * 2013-11-15 2014-04-23 安徽省绿巨人环境技术有限公司 Liquor factory high-concentration organic wastewater treatment technology
CN103739140B (en) * 2013-11-15 2016-04-20 安徽省绿巨人环境技术有限公司 A kind of Liquor factory high-concentration organic wastewater treatment technology
CN104478170A (en) * 2014-12-13 2015-04-01 周桂英 Draught beer mill wastewater treatment method and treatment device
CN104496115A (en) * 2014-12-13 2015-04-08 周桂英 Draft beer plant wastewater treatment method and treatment device
CN104529066A (en) * 2014-12-13 2015-04-22 周桂英 Method and device for treating wastewater of breweries

Similar Documents

Publication Publication Date Title
CN101234836B (en) Garbage percolate treatment technique
CN103172244B (en) Recycling treatment method of water-submerged manure in breeding industry
CN202849208U (en) Wastewater treatment system during production of white spirit
CN104478175A (en) Treatment system and method for biogas slurry produced from anaerobic fermentation of kitchen waste
CN203613071U (en) Sewage treatment device
CN103319058A (en) Traditional Chinese medicine extraction wastewater treatment system and technology
CN204958667U (en) Resident sewage treatment system
CN105110567A (en) Process for advanced treatment of southern large-scale swine wastewater
CN104829042A (en) Treatment method for printing and dyeing wastewater based on technology of facultative anaerobic membrane bioreactor
CN106517699A (en) Efficient household garbage sewage system and technology thereof
CN204417278U (en) Culturing wastewater processing system
CN104418481A (en) Mass-energy transformation treatment process for production wastewater
CN205011582U (en) Offal drainage
CN204958669U (en) Drainage of recycle -water resource
CN202063797U (en) High-concentration printing and dyeing wastewater treatment system
CN204369720U (en) Culturing wastewater processing system
CN104692585A (en) Process for treating urban domestic sewage
CN103693809B (en) Anaerobic biological treatment system for fruit juice wastewater
CN203392982U (en) High-concentration organic wastewater treatment device
CN204079590U (en) A kind of sewage generating system adopting anaerobically fermenting process
CN202849209U (en) Momordica grosvenori wastewater treatment system
CN204550333U (en) A kind of simple and easy purifying domestic sewage groove ecological treatment apparatus
CN204981502U (en) Wash a meter sewage treatment system
CN204529609U (en) Cleaning pulping wastewater treatment equipment
CN204474492U (en) Polyester waste water treatment system

Legal Events

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

Granted publication date: 20130403

Termination date: 20180920