CN202038946U - Wastewater treatment device in acrylic production process - Google Patents
Wastewater treatment device in acrylic production process Download PDFInfo
- Publication number
- CN202038946U CN202038946U CN2011201136636U CN201120113663U CN202038946U CN 202038946 U CN202038946 U CN 202038946U CN 2011201136636 U CN2011201136636 U CN 2011201136636U CN 201120113663 U CN201120113663 U CN 201120113663U CN 202038946 U CN202038946 U CN 202038946U
- Authority
- CN
- China
- Prior art keywords
- tank
- pond
- water
- aerobic
- water outlet
- 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 - Lifetime
Links
- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 17
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 title abstract 2
- 238000004519 manufacturing process Methods 0.000 title abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 47
- 238000000034 method Methods 0.000 claims abstract description 19
- 229920002972 Acrylic fiber Polymers 0.000 claims description 15
- 239000007788 liquid Substances 0.000 claims description 15
- 238000010992 reflux Methods 0.000 claims description 15
- 230000003301 hydrolyzing effect Effects 0.000 claims description 14
- 238000007380 fibre production Methods 0.000 claims description 12
- 239000004744 fabric Substances 0.000 claims description 6
- 230000009189 diving Effects 0.000 claims description 5
- 238000002955 isolation Methods 0.000 claims description 5
- 238000009434 installation Methods 0.000 claims 1
- 239000002351 wastewater Substances 0.000 abstract description 15
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 5
- 230000007062 hydrolysis Effects 0.000 abstract description 4
- 238000006460 hydrolysis reaction Methods 0.000 abstract description 4
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 4
- 229910052717 sulfur Inorganic materials 0.000 abstract description 2
- 230000001988 toxicity Effects 0.000 abstract description 2
- 231100000419 toxicity Toxicity 0.000 abstract description 2
- 230000003647 oxidation Effects 0.000 abstract 3
- 238000007254 oxidation reaction Methods 0.000 abstract 3
- 238000004062 sedimentation Methods 0.000 abstract 2
- 239000002071 nanotube Substances 0.000 abstract 1
- 239000011593 sulfur Substances 0.000 abstract 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 239000010802 sludge Substances 0.000 description 6
- 239000000945 filler Substances 0.000 description 3
- 238000001914 filtration Methods 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 230000002599 biostatic effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- JYYOBHFYCIDXHH-UHFFFAOYSA-N carbonic acid;hydrate Chemical compound O.OC(O)=O JYYOBHFYCIDXHH-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002894 chemical waste Substances 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007726 management method Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Images
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model relates to a wastewater treatment device in the acrylic production process, which is characterized in that the wastewater treatment device mainly comprises a grate, an adjusting tank, a pre-oxidation tank, a hydrolysis tank, a denitrification tank, an aerobic tank and a sedimentation tank, wherein the grate is arranged at a wastewater inlet of the adjusting tank; a water outlet of the adjusting tank is connected with a water inlet of the pre-oxidation tank through a pump; a water outlet of the pre-oxidation tank is connected with a water inlet of the hydrolysis tank; an overflow water outlet is arranged at the upper part of the side surface of the hydrolysis tank and is connected with a water inlet of the denitrification tank; a water outlet of the denitrification tank is connected with a water inlet of the aerobic tank; and a water outlet of the aerobic tank is connected with a water inlet of the sedimentation tank. The wastewater in the high-concentration process reaches the nanotube discharge requirements after being treated by the wastewater treatment device. The wastewater treatment device works stably, and has high efficiency and low running cost, effectively solves the problem of biological wastewater toxicity in the traditional treatment method and is simultaneously suitable for biological treatment of similar high-sulfur and high-nitrogen organic wastewater.
Description
Technical field
The present invention relates to a kind of acrylic fiber production process processing wastewater treatment unit, comprise grid filtration, equalizing tank, preaeration, acidication, hold concurrently oxygen denitrification and biological treatment device such as aerobic, belong to field of environment engineering.
Technical background
There are biological difficult price reduction materials such as organic sulfonate in acrylic fiber production process processing wastewater pollutent composition complexity, toxicity height, also have Biostatic components such as sulfate radical and inferior sulfate radical in addition in the waste water.In the prior art, the method for handling acrylic fiber chemical waste water mainly contains: coagulation-precipitation, coagulation-air supporting, suspension active sludge, A/O biomembrance process, biological filtering tower combined working, electrolytic process etc.The system device of these technologies, complex structure are unfavorable for operation and management, and the acrylic fibers processing wastewater is difficult to reach emission request.
The utility model content
For overcoming the defective of prior art, technical purpose of the present utility model has been to provide a kind of new acrylic fiber production process processing wastewater treatment unit, make that this device operability and security of system are good, solve the acrylic fibers processing wastewater problem completely that is difficult to carry out a biological disposal upon, reduced cost for wastewater treatment again.
The technical solution of the utility model is:
A kind of acrylic fiber production process processing wastewater treatment unit is characterized in that mainly being made up of grid, equalizing tank, preoxidation pond, hydrolytic tank, denitrification pond, Aerobic Pond, settling tank; Wherein, grid is arranged on the water intake place of equalizing tank, and the equalizing tank water outlet is by the water-in in pump connection preoxidation pond, and the water outlet in preoxidation pond connects the water-in of hydrolytic tank; The top, side of hydrolytic tank is provided with and overflows the mouth of a river, overflows the mouth of a river and is connected with denitrification pond water-in; Denitrification pond water outlet is connected with the Aerobic Pond water-in, and the Aerobic Pond water outlet is connected with the settling tank water-in.
Wherein, described preoxidation pond also is provided with settling tank mud refluxing opening; Described settling tank go out the mud mouth connects the preoxidation pond by pump settling tank mud refluxing opening.
The diving whipping appts is installed in described hydrolytic tank and bottom, denitrification pond.
Described denitrification pond also is provided with the nitrification liquid reflux inlet; Aerobic Pond also is provided with the nitrification liquid bypass outlet; The nitrification liquid bypass outlet of Aerobic Pond connects the nitrification liquid reflux inlet in denitrification pond by pump.
Described Aerobic Pond is divided into one section Aerobic Pond and two sections Aerobic Ponds, the Aerobic Pond water-in is one section Aerobic Pond water-in, one section Aerobic Pond water outlet is two sections Aerobic Pond water-ins, two sections Aerobic Pond water outlets are the Aerobic Pond water outlet, and wherein the water-in of one section Aerobic Pond and water outlet are provided with the isolation screen cloth.
Described settling tank water-in is provided with the inlet distribution device.
The beneficial effects of the utility model are:
This utility model has adopted grid, equalizing tank, preoxidation pond, hydrolysis acidification pool, hold concurrently oxygen denitrification pond and aerobic nitrification tank series connection processing waste water, S, C, N classification are removed, improved the biological treatment performance, water outlet COD and TN are lower, based on biotechnology, technical process is reasonable, and running cost is low.After double oxygen is handled two sections aerobic process are set, first section adds bio-carrier, improves activated sludge concentration, and waste water COD is effectively removed.System works is stable, and treatment effect is good.The utility model is equally applicable to the biological treatment of other high-sulfurs, high nitrogen organic waste water.
Description of drawings
Fig. 1 is the utility model synoptic diagram.
Embodiment
As shown in Figure 1, acrylic fiber production process processing wastewater treatment unit described in the utility model mainly is made up of grid, equalizing tank, preoxidation pond, hydrolytic tank, denitrification pond, Aerobic Pond, settling tank; Wherein, grid is arranged on the water intake place of equalizing tank, and the equalizing tank water outlet is by the water-in in pump connection preoxidation pond, and the water outlet in preoxidation pond connects the water-in of hydrolytic tank; The top, side of hydrolytic tank is provided with and overflows the mouth of a river, overflows the mouth of a river and is connected with denitrification pond water-in; Denitrification pond water outlet is connected with the Aerobic Pond water-in, and the Aerobic Pond water outlet is connected with the settling tank water-in.
Wherein, described preoxidation pond also is provided with settling tank mud refluxing opening; Described settling tank go out the mud mouth connects the preoxidation pond by pump settling tank mud refluxing opening.
The diving whipping appts is installed in described hydrolytic tank and bottom, denitrification pond.
Described denitrification pond also is provided with the nitrification liquid reflux inlet; Aerobic Pond also is provided with the nitrification liquid bypass outlet; The nitrification liquid bypass outlet of Aerobic Pond connects the nitrification liquid reflux inlet in denitrification pond by pump.
Described Aerobic Pond is divided into one section Aerobic Pond and two sections Aerobic Ponds, the Aerobic Pond water-in is one section Aerobic Pond water-in, one section Aerobic Pond water outlet is two sections Aerobic Pond water-ins, two sections Aerobic Pond water outlets are the Aerobic Pond water outlet, wherein the water-in of one section Aerobic Pond and water outlet are provided with the isolation screen cloth, and add the carrier organism filler at one section Aerobic Pond.
Described settling tank water-in is provided with the inlet distribution device.
During operation, waste water is promoted to the preoxidation pond by lift pump inherent regulation pond, and the preoxidation pond also is provided with settling tank mud refluxing opening; When system moved, settling tank mud was through mud reflux input preoxidation pond, and returned sluge replenishes preoxidation pond sludge concentration.Hydrolytic tank is provided with the diving whipping appts and overflows the mouth of a river, overflows the mouth of a river and is connected with denitrification pond water-in.The macromole organic pollutant is broken down into small-molecule substance in hydrolytic tank.The denitrification pond is provided with diving whipping appts and water outlet, also is provided with one section aerobic nitrification liquid reflux, and double oxygen reaction takes place for acidication water outlet and aerobic nitrification liquid, removes the nitrogen in the waste water.The oxygen denitrification water outlet of holding concurrently is connected with one section aerobic nitrification pond water-in, and the centre is provided with the isolation screen cloth, and one section aerobic nitrification pond adds the carrier organism filler.One section aerobic nitrification pond water outlet is connected with two sections aerobic nitrification pond water-ins, and the centre is provided with the isolation screen cloth.Two sections aerobic nitrification pond water outlets are connected with the settling tank water-in, and the settling tank water-in is provided with the inlet distribution system.It is the loss that prevents the carrier organism filler that one section aerobic nitrification pond entery and delivery port is provided with the purpose of isolating screen cloth, and one section, two sections aerobic nitrification ponds are provided with blast aeration system simultaneously, and organism exists in the waste water.The oxygen denitrification water outlet of holding concurrently is progressively decomposed by microorganism in one section, two sections aerobic nitrification ponds, generates carbonic acid gas and water in microbial reproduction.Waste water after carrying out a biological disposal upon in settling tank solid-liquid separation, part mud is back to preaeration tank, replenishes the preaeration tank sludge concentration, excess sludge discharge is to sludge treating system, waste water is to discharging the pond.
Claims (6)
1. an acrylic fiber production process processing wastewater treatment unit is characterized in that mainly being made up of grid, equalizing tank, preoxidation pond, hydrolytic tank, denitrification pond, Aerobic Pond, settling tank; Wherein, grid is arranged on the water intake place of equalizing tank, and the equalizing tank water outlet is by the water-in in pump connection preoxidation pond, and the water outlet in preoxidation pond connects the water-in of hydrolytic tank; The top, side of hydrolytic tank is provided with and overflows the mouth of a river, overflows the mouth of a river and is connected with denitrification pond water-in; Denitrification pond water outlet is connected with the Aerobic Pond water-in, and the Aerobic Pond water outlet is connected with the settling tank water-in.
2. acrylic fiber production process processing wastewater treatment unit according to claim 1 is characterized in that described preoxidation pond also is provided with settling tank mud refluxing opening; Described settling tank go out the mud mouth connects the preoxidation pond by pump settling tank mud refluxing opening.
3. acrylic fiber production process processing wastewater treatment unit according to claim 1 is characterized in that described hydrolytic tank and denitrification pond bottom installation diving whipping appts.
4. acrylic fiber production process processing wastewater treatment unit according to claim 1 is characterized in that described denitrification pond also is provided with the nitrification liquid reflux inlet; Aerobic Pond also is provided with the nitrification liquid bypass outlet; The nitrification liquid bypass outlet of Aerobic Pond connects the nitrification liquid reflux inlet in denitrification pond by pump.
5. acrylic fiber production process processing wastewater treatment unit according to claim 1, it is characterized in that described Aerobic Pond is divided into one section Aerobic Pond and two sections Aerobic Ponds, the Aerobic Pond water-in is one section Aerobic Pond water-in, one section Aerobic Pond water outlet is two sections Aerobic Pond water-ins, two sections Aerobic Pond water outlets are the Aerobic Pond water outlet, and wherein the water-in of one section Aerobic Pond and water outlet are provided with the isolation screen cloth.
6. acrylic fiber production process processing wastewater treatment unit according to claim 1 is characterized in that described settling tank water-in is provided with the inlet distribution device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201136636U CN202038946U (en) | 2011-04-18 | 2011-04-18 | Wastewater treatment device in acrylic production process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201136636U CN202038946U (en) | 2011-04-18 | 2011-04-18 | Wastewater treatment device in acrylic production process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202038946U true CN202038946U (en) | 2011-11-16 |
Family
ID=44966403
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201136636U Expired - Lifetime CN202038946U (en) | 2011-04-18 | 2011-04-18 | Wastewater treatment device in acrylic production process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202038946U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102765857A (en) * | 2012-08-06 | 2012-11-07 | 上海电力学院 | Sewage treatment system and application thereof |
| CN103086576A (en) * | 2013-02-28 | 2013-05-08 | 北京凯易信环境科技有限公司 | Acrylonitrile/acrylon production comprehensive wastewater treatment technique |
| CN105242696A (en) * | 2015-10-23 | 2016-01-13 | 蓝星石油有限公司济南分公司 | Sewage treatment monitoring pond effluent control system |
-
2011
- 2011-04-18 CN CN2011201136636U patent/CN202038946U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102765857A (en) * | 2012-08-06 | 2012-11-07 | 上海电力学院 | Sewage treatment system and application thereof |
| CN103086576A (en) * | 2013-02-28 | 2013-05-08 | 北京凯易信环境科技有限公司 | Acrylonitrile/acrylon production comprehensive wastewater treatment technique |
| CN105242696A (en) * | 2015-10-23 | 2016-01-13 | 蓝星石油有限公司济南分公司 | Sewage treatment monitoring pond effluent control system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102531298B (en) | Sewage treatment device and method for enhanced denitrification A/A/O (Anodic Aluminum Oxide) and deoxygenation BAF (Biological Aerated Filter) | |
| CN203866154U (en) | Low-energy-consumption stepped sewage treatment device | |
| CN202089869U (en) | High-efficient composite reaction device for anaerobic organism | |
| CN102976566B (en) | System and method for treating high-concentration landfill leachate in aerobic composting site | |
| CN101591123A (en) | A kind of printing and dyeing wastewater treatment system | |
| CN103979732B (en) | The film biological treating equipment of methane and sulfur-bearing nitrogenous effluent associated treatment and method thereof | |
| CN106630150B (en) | Drop oxygen-enriched oxygen sludge bed process and its wastewater treatment method of declining | |
| CN202390287U (en) | Internal iron-carbon UASB-SBR (Upflow Anaerobic Sludge Blanket-Sequencing Batch Reactor) coupling system for treatment of printing and dyeing wastewater | |
| CN102942285A (en) | Sewage treatment system and method for natural gas purifying factory in H2S-containing gas field | |
| CN100484886C (en) | Process for treatnig paper-making waste water of waste paper | |
| CN204211537U (en) | The double oxygen MBR membrane bioreactor of integration | |
| CN202038946U (en) | Wastewater treatment device in acrylic production process | |
| CN108314255A (en) | A kind of efficient Chinese herbal medicine extraction sewage treatment process | |
| CN202988918U (en) | Multi-stage multi-section combined type high concentration chemical wastewater treatment system | |
| CN202063797U (en) | High-concentration printing and dyeing wastewater treatment system | |
| CN104445838A (en) | Sewage treatment system for small towns | |
| CN203392982U (en) | High-concentration organic wastewater treatment device | |
| CN208136048U (en) | A kind of vegetables juicing waste water treatment system | |
| CN203269735U (en) | Equipment for treating rubbish leachate by utilizing two-stage bioreactors | |
| CN103601298B (en) | Membrane bioreactor technology as well as device thereof based on pollutant parallel processing | |
| CN205328795U (en) | Wet spinning acrylic fibres production polymerization effluent disposal system | |
| CN209468196U (en) | One kind being based on A2The vertical integrated sewage disposal device of/O technique | |
| CN203602404U (en) | Membrane bioreactor device based on parallel pollutant treatment | |
| CN202430086U (en) | Device for synthesizing and treating landfill leachate | |
| CN208814846U (en) | Oil-contained waste water treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 210047, -155, No. 168, Tai Chi Road, Nanjing chemical industry park, Liuhe, Jiangsu Patentee after: PURITEK ENVIRONMENT GROUP CO.,LTD. Address before: 210009 218, Building 4, Industrial Design and Entrepreneurship Park, Nanjing Tech University, 200 Zhongshan North Road, Nanjing, Jiangsu Province Patentee before: PURITEK (NANJING) CO.,LTD. |
|
| CP03 | Change of name, title or address | ||
| CX01 | Expiry of patent term |
Granted publication date: 20111116 |
|
| CX01 | Expiry of patent term |