CN210711146U - Sugar industry effluent treatment plant - Google Patents
Sugar industry effluent treatment plant Download PDFInfo
- Publication number
- CN210711146U CN210711146U CN201921211672.1U CN201921211672U CN210711146U CN 210711146 U CN210711146 U CN 210711146U CN 201921211672 U CN201921211672 U CN 201921211672U CN 210711146 U CN210711146 U CN 210711146U
- Authority
- CN
- China
- Prior art keywords
- tank
- tlp
- wastewater
- sugar
- anaerobic reactor
- 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
Links
Images
Abstract
The utility model relates to a sugar industry effluent treatment plant, including oil interceptor, cooling tower, acidizing jar, equalizing basin, TLP anaerobic reactor, settling cask, neutralization pond, oxidation ditch and the sedimentation tank that communicates in proper order, the other charge device that is provided with of equalizing basin is equipped with the elevator pump between equalizing basin and the TLP anaerobic reactor, the gas outlet of oxidation ditch in-connection air-blast aeration machine. The treatment method comprises the steps of sequentially treating the high-concentration sugar-making industrial wastewater by an oil separation tank, a cooling tower, an acidification tank, a regulating tank, a TLP (TLP) anaerobic reactor and a settling tank to reduce the concentration of the high-concentration sugar-making industrial wastewater, mixing the high-concentration sugar-making industrial wastewater with the low-concentration sugar-making industrial wastewater, and performing aerobic biochemical treatment on the mixed wastewater. The device is used for wastewater treatment, can digest and degrade organic matters, realizes standard discharge of wastewater, and reduces energy consumption and operation cost.
Description
Technical Field
The utility model relates to an environmental protection technology field particularly, relates to a sugaring industrial wastewater treatment device.
Background
Water shortage and serious water body environmental pollution in China require the total discharge amount of pollutants of sugar-making wastewater and the standard discharge of water pollution indexes. The prior sugar industry wastewater treatment method mainly adopts aerobic biochemical treatment, such as activated sludge and a biofilm method. However, the management is not good in the production process, sugar and sugar are easy to carry, the concentration of COD pollutants in the waste water after sugar is carried out is generally more than 1500mg/L, and is often 2-3 times higher than the COD value of the inlet water designed by an aerobic biochemical system, and organic matters cannot be completely digested and degraded. Most enterprises mix and dilute high-concentration sugar-making wastewater and clear water into low concentration, and then adopt aerobic biochemical treatment, so that organic matters can be digested and degraded, and the wastewater reaches the standard and is discharged; but the treatment process needs a large amount of clear water and a large amount of treatment devices, so that the energy consumption and the operation cost are increased, and the treatment capacity is also reduced.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a sugaring industry effluent treatment plant to the above-mentioned defect among the prior art.
In order to realize the above purpose, the utility model provides a sugar industry effluent treatment plant, including oil interceptor, cooling tower, acidizing jar, equalizing basin, TLP anaerobic reactor, settling cask, neutralization pond, oxidation ditch and the sedimentation tank that communicates in proper order, the other charge device that is provided with of equalizing basin is equipped with the elevator pump between equalizing basin and the TLP anaerobic reactor, the gas outlet of oxidation ditch in-connection blast aeration machine.
The sugar industry wastewater treatment device also comprises a sludge concentration tank and a filter press, wherein a sludge port of the sedimentation tank is connected with an inlet of the sludge concentration tank, and an outlet of the sludge concentration tank is connected with an inlet of the filter press. The sludge concentration tank and the filter press are used for removing the moisture of the sludge, so that the volume of the sludge is reduced, and the subsequent treatment cost of the sludge is reduced.
Return pipes are communicated between the TLP anaerobic reactor and the settling tank and between the oxidation ditch and the sedimentation tank.
Compared with the prior art, the utility model has the advantages that:
the utility model discloses a system sugar industrial wastewater treatment device is rationally distributed, uses the device to carry out system sugar industrial wastewater treatment, handles high concentration system sugar industrial wastewater through oil interceptor, cooling tower, acidizing jar, equalizing basin, TLP anaerobic reactor and settling cask earlier in proper order, makes the concentration of high concentration system sugar industrial wastewater reduce, then mixes the back with low concentration system sugar industrial wastewater again, and the waste water that mixes the gained adopts good oxygen biochemical treatment. After being subjected to acidification hydrolysis and anaerobic digestion, the high-concentration sugar-making industrial wastewater is mixed with the low-concentration wastewater and then subjected to aerobic biochemical treatment, so that organic matters can be digested and degraded, and the wastewater is discharged after reaching the standard; compared with the method of mixing by introducing clean water, the method does not need to invest a large amount of equipment and energy for mixing and diluting, reduces energy consumption and operation cost, and improves treatment capacity.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings used in the embodiments or the related art descriptions will be briefly described below.
FIG. 1 is a block diagram showing the structure of a wastewater treatment apparatus in sugar industry
Detailed Description
In order to make the aforementioned objects, features and advantages of the present invention more clearly understood, the following detailed description of the present invention, taken in conjunction with the accompanying drawings and the detailed description, is given in a non-limiting manner.
As shown in figure 1, the sugar-making industrial wastewater treatment device comprises an oil separation tank, a cooling tower, an acidification tank, a regulating tank, a TLP anaerobic reactor, a settling tank, a neutralization tank, an oxidation ditch and a sedimentation tank which are sequentially communicated, wherein a dosing device is arranged beside the regulating tank, a lift pump is arranged between the regulating tank and the TLP anaerobic reactor, and an air outlet of a blast aerator is communicated in the oxidation ditch. The sugar industry wastewater treatment device also comprises a sludge concentration tank and a filter press, wherein a sludge port of the sedimentation tank is connected with an inlet of the sludge concentration tank, and an outlet of the sludge concentration tank is connected with an inlet of the filter press. Return pipes are communicated between the TLP anaerobic reactor and the settling tank and between the oxidation ditch and the sedimentation tank.
The specific steps of using the sugar industry wastewater treatment device to treat wastewater are as follows: introducing the high-concentration sugar-making industrial wastewater into an oil separation tank to remove suspended oil and heavy oil. Then sequentially entering a cooling tower to be cooled to the hydrolysis temperature, entering an acidification tank to be hydrolyzed, entering an adjusting tank to adjust the pH value to be neutral, entering a TLP anaerobic reactor to be subjected to anaerobic decomposition, and entering a settling tank to be subjected to first mud-water separation; supernatant obtained by the first mud-water separation enters a neutralization tank, and low-concentration sugar-making industrial wastewater is introduced into the neutralization tank for mixing; and (3) the mixed wastewater enters an oxidation ditch, activated sludge is utilized for carrying out catabolism, and then the wastewater enters a sedimentation tank for carrying out secondary mud-water separation, so that clear water which can reach the standard discharge is obtained. In the wastewater treatment process, the wastewater condition in the regulating tank is checked regularly, and if the flocs in the tank are small, the chemical adding device needs to be opened to ensure that the pH value of the wastewater passing through the regulating tank is neutral.
It should be noted that the above-mentioned preferred embodiments are only for illustrating the technical concepts and features of the present invention, and the purpose thereof is to enable those skilled in the art to understand the contents of the present invention and to implement the present invention accordingly, and the protection scope of the present invention cannot be limited thereby. All equivalent changes and modifications made according to the spirit of the present invention should be covered by the protection scope of the present invention.
Claims (3)
1. The utility model provides a sugar industry effluent treatment plant which characterized in that: the device comprises an oil separation tank, a cooling tower, an acidification tank, a regulating tank, a TLP (TLP) anaerobic reactor, a settling tank, a neutralization tank, an oxidation ditch and a sedimentation tank which are sequentially communicated, wherein a dosing device is arranged beside the regulating tank, a lift pump is arranged between the regulating tank and the TLP anaerobic reactor, and an air outlet of a blast aerator is communicated in the oxidation ditch.
2. The sugar industry wastewater treatment plant of claim 1, characterized in that:
the sludge treatment device is characterized by further comprising a sludge concentration tank and a filter press, wherein a sludge port of the sedimentation tank is connected with an inlet of the sludge concentration tank, and an outlet of the sludge concentration tank is connected with an inlet of the filter press.
3. The sugar industry wastewater treatment plant of claim 1, characterized in that:
return pipes are communicated between the TLP anaerobic reactor and the settling tank and between the oxidation ditch and the sedimentation tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201921211672.1U CN210711146U (en) | 2019-07-30 | 2019-07-30 | Sugar industry effluent treatment plant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201921211672.1U CN210711146U (en) | 2019-07-30 | 2019-07-30 | Sugar industry effluent treatment plant |
Publications (1)
Publication Number | Publication Date |
---|---|
CN210711146U true CN210711146U (en) | 2020-06-09 |
Family
ID=70960358
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201921211672.1U Expired - Fee Related CN210711146U (en) | 2019-07-30 | 2019-07-30 | Sugar industry effluent treatment plant |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN210711146U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110357363A (en) * | 2019-07-30 | 2019-10-22 | 南宁职业技术学院 | A kind of sugar industry wastewater processing unit and method |
-
2019
- 2019-07-30 CN CN201921211672.1U patent/CN210711146U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110357363A (en) * | 2019-07-30 | 2019-10-22 | 南宁职业技术学院 | A kind of sugar industry wastewater processing unit and method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN109721158B (en) | Device and method for treating late landfill leachate by using semi-shortcut nitrification/double anaerobic ammonia oxidation process | |
CN106830562B (en) | Petrochemical industry industrial wastewater treatment integrated process system and method | |
CN210711175U (en) | Kitchen garbage anaerobic digestion waste water non-membrane method processing system | |
CN103466885A (en) | Process for treating wastewater generated in solar silicon wafer production process | |
CN101838083A (en) | Method for treating organic chemical wastewater having high COD and high concentration of sulfate ions | |
CN202089870U (en) | Biological treatment device for hydroxyethyl cellulose industrial waste water | |
CN203065303U (en) | Meat-packing sewage treatment system | |
CN105399285B (en) | A kind of sludge reduction sewage water treatment method | |
CN103408201A (en) | Treatment method of industrial wastewater in silicon wafer mortar recovery | |
CN109133524A (en) | The processing system and processing method of high COD medicine intermediate wastewater from chemical industry with high salt | |
CN111410362A (en) | Method for treating coffee primary processing wastewater | |
CN202297315U (en) | Dedicated device for wastewater treatment of phenolic resin | |
CN210711146U (en) | Sugar industry effluent treatment plant | |
CN109626639A (en) | A kind of processing method of high concentration organism P wastewater | |
CN101962248A (en) | Treatment method for biological total nitrogen removal | |
CN103304076A (en) | Catalytic micro-electrolysis water treatment equipment and process method thereof | |
CN216236438U (en) | Pretreatment system for garbage extrusion leachate | |
CN204529599U (en) | A kind of sewage disposal device | |
CN210237393U (en) | Sinomenine hydrochloride production sewage treatment system | |
CN210711177U (en) | Pig manure fermentation biogas slurry treatment system | |
CN1327039C (en) | Technology for treating electroplating effluent by biochemical process | |
CN209974510U (en) | Sulfur-containing urea wastewater treatment device | |
CN208218604U (en) | A kind of high-concentration hardly-degradable industrial wastewater treatment system | |
CN212050998U (en) | Cassava starch effluent treatment plant | |
CN101402502B (en) | Treatment method and apparatus for mifepristone wastewater |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
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: 20200609 Termination date: 20210730 |