CN201864633U - Sausage casing heparin wastewater treatment system - Google Patents
Sausage casing heparin wastewater treatment system Download PDFInfo
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- CN201864633U CN201864633U CN2010205880791U CN201020588079U CN201864633U CN 201864633 U CN201864633 U CN 201864633U CN 2010205880791 U CN2010205880791 U CN 2010205880791U CN 201020588079 U CN201020588079 U CN 201020588079U CN 201864633 U CN201864633 U CN 201864633U
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Abstract
The utility model relates to a sausage casing heparin wastewater treatment system which comprises a water collecting pond, a rough-filtering jar and a micro-filtering jar, wherein the rough-filtering jar is arranged below the side of the water collecting pond, a pipeline communicated with the top of the rough-filtering jar is arranged on the side wall at the upper part of the water collecting pond, and a plate frame filled with the active carbon is arranged in the middle of the rough-filtering jar; a micro-filtering jar body is internally provided with a plurality of organic micro-filtering membranes and organic ultra-filtering membranes, the organic micro-filtering membranes are arranged at the upper part of the jar body, and the organic ultra-filtering membranes are arranged at the lower part of the jar body; and the rough-filtering jar is connected with the micro-filtering jar by a pressurizing pump, a water inlet of the pressurizing pump is communicated with the bottom of the rough-filtering jar, and a water outlet of the pressurizing pump is communicated with a water inlet of a membrane filtering jar. The sausage casing heparin wastewater is stored in the water collecting pond, the flocculated wastewater at the upper part of the water collecting pond flows into the rough-filtering jar, the particulates of the wastewater are reabsorbed by the active carbon, the wastewater is pumped into the membrane filtering jar by the pressurizing pump, and the particulates and the other pollutants are baffled under the action of the filtering membranes, so that an aim for purifying the wastewater is achieved, therefore, the purified wastewater can be led into an industrial water recycle system by a water pump for recycling.
Description
Technical field
The utility model relates to a kind of Waste Water Treatment, particularly a kind of casing heparin Waste Water Treatment.
Background technology
Casing is the traditional large livestock product of outlet of China, is positioned at the first five position of the export of farm produce for many years always.Because the small intestine aboundresources, heparin content is also higher in its mucous membrane, and at present, the domestic mucous membrane of small intestine waste that scrapes in the casing course of processing that mostly utilizes extracts heparin sodium as raw material.More than 100 ton of China's annual outlet heparin and heparin sodium are that the main supply of world's heparin raw material is national.It is estimated that China's casing processing waste water quantity discharged is 2250 ~ 7500t/d, the about 6000t/d of heparin processing waste water.
Casing waste water belongs to organic waste water, the organism, particularly its chemical oxygen demand (COD) (COD that easily are degraded by microorganisms because of the amino acid that wherein contains some amount, fat etc.
CrValue) very high, scope is between 625 ~ 2100mg/L, and directly discharging very easily causes the pollution to surrounding environment.
The utility model content
The technical problems to be solved in the utility model provides a kind of system that casing heparin waste water is handled recycling.
For solving the problems of the technologies described above, the technical solution of the utility model is: a kind of casing heparin Waste Water Treatment, and its innovative point is: comprise a water collecting basin, this water collecting basin top is provided with the flocculation agent filling tube; One coarse filtration jar, this coarse filtration jar is positioned at the water collecting basin side-lower, and the water collecting basin upper portion side wall is provided with the pipeline that is communicated with the coarse filtration tank top, and the middle part of coarse filtration jar is provided with a sheet frame that is filled with activated carbon; One micro-filtration jar is provided with the organic microfiltration membrane of some tubuloses in this micro-filtration jar, the top of micro-filtration jar have with organic microfiltration membrane pipe in the water-in that is communicated with, the bottom has water port; One ultrafiltration jar is provided with the organic ultra-filtration membrane of some tubuloses in this ultrafiltration jar, the top of ultrafiltration jar have with organic ultrafiltration membrane pipe in the water-in that is communicated with, the bottom has water port; Connect by two topping-up pumps between coarse filtration jar, micro-filtration jar, the ultrafiltration jar three, the water-in of first topping-up pump is communicated with the coarse filtration pot bottom, water outlet is communicated with micro-filtration tank top water-in, the water-in of second topping-up pump is communicated with micro-filtration pot bottom water port, and water outlet is communicated with ultrafiltration tank top water-in.
Further, described water collecting basin is an enclosed construction, its center, top is equipped with agitator, water collecting basin one side is provided with the deodorizing jar, this deodorizing jar is communicated with water collecting basin by pipeline, be built-in with the air inducing fan in described pipeline, evenly be fixed with some flase floors in the deodorizing tank from top to bottom, support has the filler that is attached with microbial strains on the described flase floor.
Further, described agitator has two agitating vanes, and blade is separately fixed at the upper and lower part of stir shaft, and is coaxial crossing at right angle arrangement.
Advantage of the present utility model is: casing heparin waste water is stored in the water collecting basin, adds flocculation agent in water collecting basin, makes waste water small particles suspended particulates be coupled to thick cotton-shaped or agglomerate.The waste water on water collecting basin top flows into the coarse filtration jar, through activated carbon once more after the adsorbent particles by two topping-up pumps suction micro-filtration jar successively and ultrafiltration jar, under the effect of its organic microfiltration membrane and organic ultra-filtration membrane, hold back particulate and other pollutents, to reach the purpose of purifying liquid waste, the waste water after the purification can be introduced the process water recycle system by water pump and carry out cycling and reutilization.Day to handle 100 tons of calculating of waste water, take all factors into consideration direct working cost, depreciation funds and maintenance funds, about 0.8 yuan of the processing costs of waste water per ton; Year is saved 20000 tons of waters, by 2.6 yuan/ton, is worth 5.2 ten thousand yuan.Reduce sewage emissions, alleviate, improve people's living environment the pollution of water body on every side.
The pond body is an enclosed construction, and, can remove the peculiar smell that waste water gives out, and carry out the stirring of flocculation agent and waste water by agitator when stirring at the deodorizing jar that body one side setting in pond is communicated with it, guarantee can not smell when the workman works the peculiar smell of waste water, improved workman's Working environment.Mixing utensil has two agitating vanes, and blade is separately fixed at the upper and lower part of stir shaft, is coaxial crossing at right angle and arranges, and mixing effect is good, has improved the efficient of pre-treatment greatly.
Description of drawings
Accompanying drawing is the utility model casing heparin Waste Water Treatment structural representation.
Embodiment
As shown in drawings, comprise water collecting basin 1, flocculation agent filling tube 2, agitator 11, deodorizing jar 12, pipeline 13, air inducing fan 14, flase floor 15, coarse filtration jar 3, activated carbon 4, micro-filtration jar 5, microfiltration membrane 7, ultrafiltration jar 6, ultra-filtration membrane 8, first topping-up pump 9, second topping-up pump 10.
Above-mentioned water collecting basin 1 top is provided with flocculation agent filling tube 2, and water collecting basin 1 is an enclosed construction, and its center, top is equipped with agitator 11, and this agitator 11 has two agitating vanes, and blade is separately fixed at the upper and lower part of stir shaft, and is coaxial crossing at right angle arrangement.
Side-lower at water collecting basin 1 is provided with a coarse filtration jar 3, and these coarse filtration jar 3 tops are communicated with by pipeline 4 with the upper portion side wall of water collecting basin 1, and coarse filtration jar 3 middle parts are provided with a sheet frame, are filled with activated carbon 4 in the sheet frame.
The tank body top and the bottom of micro-filtration jar 5 are driven the mouth of a river, water port respectively into, are provided with several organic microfiltration membrane 7 in the tank body, the tubulose of the densely covered micropore of its structure tube wall, and the membrane pore size scope is at 0.1～1 micron.
The tank body top and the bottom of ultrafiltration jar 6 are driven the mouth of a river, water port respectively into, are provided with several organic ultra-filtration membranes 8 in the tank body, the tubulose of the densely covered ultramicropore of its structure tube wall, and membrane pore size is between 0.05um to 1000um molecular weight.
Connect by two topping-up pumps 9,10 between coarse filtration jar 3, micro-filtration jar 5, ultrafiltration jar 6 threes, the water-in of first topping-up pump 9 is communicated with coarse filtration jar 3 bottoms, water outlet is communicated with micro-filtration jar 5 top water-ins, the water-in of second topping-up pump 10 is communicated with micro-filtration jar 5 bottom discharge mouths, and water outlet is communicated with ultrafiltration jar 6 top water-ins.The water outlet of ultrafiltration jar 6 bottoms can insert the water of productive use system of casing heparin by pump.
Casing heparin waste water at first is stored in the water collecting basin 1, adds the flocculation agent of doses by flocculation agent filling tube 2 in water collecting basin 1, makes waste water small particles suspended particulates be coupled to thick cotton-shaped or agglomerate.The waste water on water collecting basin 1 top flows into coarse filtration jar 3, through activated carbon 4 once more after the adsorbent particles by topping-up pump 8 suction micro-filtration jars 5, under the effect of its organic microfiltration membrane 6 and organic ultra-filtration membrane 7, hold back particulate and other pollutents, to reach the purpose of purifying liquid waste, the waste water after the purification can be introduced the casing heparin by water pump and carry out cycling and reutilization with water circulation system.
Claims (3)
1. a casing heparin Waste Water Treatment is characterized in that: comprise
One water collecting basin, this water collecting basin top is provided with the flocculation agent filling tube;
One coarse filtration jar, this coarse filtration jar is positioned at the water collecting basin side-lower, and the water collecting basin upper portion side wall is provided with the pipeline that is communicated with the coarse filtration tank top, and the middle part of coarse filtration jar is provided with a sheet frame that is filled with activated carbon;
One micro-filtration jar is provided with the organic microfiltration membrane of some tubuloses in this micro-filtration jar, the top of micro-filtration jar have with organic microfiltration membrane pipe in the water-in that is communicated with, the bottom has water port;
One ultrafiltration jar is provided with the organic ultra-filtration membrane of some tubuloses in this ultrafiltration jar, the top of ultrafiltration jar have with organic ultrafiltration membrane pipe in the water-in that is communicated with, the bottom has water port;
Connect by two topping-up pumps between coarse filtration jar, micro-filtration jar, the ultrafiltration jar three, the water-in of first topping-up pump is communicated with the coarse filtration pot bottom, water outlet is communicated with micro-filtration tank top water-in, the water-in of second topping-up pump is communicated with micro-filtration pot bottom water port, and water outlet is communicated with ultrafiltration tank top water-in.
2. casing heparin Waste Water Treatment according to claim 1 is characterized in that: described water collecting basin is an enclosed construction, and its center, top is equipped with agitator; Water collecting basin one side is provided with the deodorizing jar, this deodorizing jar is communicated with water collecting basin by pipeline, be built-in with the air inducing fan in described pipeline, evenly be fixed with some flase floors in the deodorizing tank from top to bottom, support has the filler that is attached with microbial strains on the described flase floor.
3. casing heparin Waste Water Treatment according to claim 2 is characterized in that: described agitator has two agitating vanes, and blade is separately fixed at the upper and lower part of stir shaft, and is coaxial crossing at right angle arrangement.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205880791U CN201864633U (en) | 2010-11-03 | 2010-11-03 | Sausage casing heparin wastewater treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205880791U CN201864633U (en) | 2010-11-03 | 2010-11-03 | Sausage casing heparin wastewater treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201864633U true CN201864633U (en) | 2011-06-15 |
Family
ID=44135795
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205880791U Expired - Fee Related CN201864633U (en) | 2010-11-03 | 2010-11-03 | Sausage casing heparin wastewater treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201864633U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102690026A (en) * | 2012-06-18 | 2012-09-26 | 哈尔滨工业大学 | Method for treating waste water generated in casing production |
| CN106745910A (en) * | 2017-02-28 | 2017-05-31 | 四川建筑职业技术学院 | A kind of sewage disposal separator |
| CN108706767A (en) * | 2018-05-31 | 2018-10-26 | 江苏天航水处理有限公司 | Heavy metal-polluted water process reaction unit |
| CN110818193A (en) * | 2019-11-20 | 2020-02-21 | 徐州市国栋生化装备有限公司 | Industrial wastewater biofilm multistage treatment device and use method thereof |
-
2010
- 2010-11-03 CN CN2010205880791U patent/CN201864633U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102690026A (en) * | 2012-06-18 | 2012-09-26 | 哈尔滨工业大学 | Method for treating waste water generated in casing production |
| CN106745910A (en) * | 2017-02-28 | 2017-05-31 | 四川建筑职业技术学院 | A kind of sewage disposal separator |
| CN108706767A (en) * | 2018-05-31 | 2018-10-26 | 江苏天航水处理有限公司 | Heavy metal-polluted water process reaction unit |
| CN110818193A (en) * | 2019-11-20 | 2020-02-21 | 徐州市国栋生化装备有限公司 | Industrial wastewater biofilm multistage treatment device and use method thereof |
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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: 20110615 Termination date: 20161103 |