CN105481184B - Food and drink waste water handles retracting device and method - Google Patents
Food and drink waste water handles retracting device and method Download PDFInfo
- Publication number
- CN105481184B CN105481184B CN201511030623.4A CN201511030623A CN105481184B CN 105481184 B CN105481184 B CN 105481184B CN 201511030623 A CN201511030623 A CN 201511030623A CN 105481184 B CN105481184 B CN 105481184B
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- waste water
- sewage
- water
- filtering
- biochemistry pool
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Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
Abstract
The present invention relates to industrial wastewater treatment device and technology field,Specifically a kind of non-secondary pollution,Food and drink waste water processing retracting device of reasonable cost and method,It is characterized in that equipped with for separating the separate tank of bulk foreign matter and sewage in waste water,For the pulverizer crushed to the bulk foreign matter isolated,For foreign matter after crushing to be put into the transport mechanism of biochemistry pool,For carrying out the sedimentation basin of precipitation filtering to waste water after separation,For carrying out the ozone oxidation mechanism of oxygenolysis to filtrate after precipitation,The aeration tank of Air Exposure is carried out for the sewage after being decomposed to ozone oxidation,The filtering that filtration treatment is carried out for sewage after being decomposed to biochemistry pool precipitates mechanism,The present invention is compared with prior art,Acidic materials need not be added in sewage disposal process or alkaline matter is adjusted sewage,Do not produce secondary pollution,Waste residue and waste water can recycle after processing,It is low with cost,Working stability,The advantages that environment-protection low-consumption.
Description
Technical field：
The present invention relates to industrial wastewater treatment device and technology field, specifically a kind of non-secondary pollution, into
This rational food and drink waste water processing retracting device and method.
Background technology：
With flourishing for catering industry, the discharge capacity of food and drink waste water is increasing, it has also become a weight of town sewage
Source is wanted, its discharge capacity accounts for the 3% of municipal wastewater discharge capacity.But food and drink waste water COD and BOD5Contribution margin but to have reached 1/3 left
It is right.This is because the high organic content of food and drink waste water, composition is sufficiently complex, mainly there is food fiber, starch, fat, dynamic plant
Thing grease, all kinds of seasonings, detergent and protein etc..Therefore, the below standard discharge of food and drink waste water can not only increase municipal wastewater
The load of processing, moreover, certain pollution will be produced to surrounding city river；In addition, the swill in food and drink waste water easily blocks up
Sewer and urban sewage pipe are filled in, and distributes niff, under the conditions of long term hypoxia, food and drink waste water also easily arrange by corrosion
Waterpipe.
Food and drink waste water is caused leftover and water during food and drink, with starch, food fiber class, tallow
The organic matters such as fat class are main component, have high organic content, pH excursions are big, moisture content is high, perishable fermentation is smelly etc.
Feature, it has also become one of city pollution sources of greatest concern.At present, food and drink waste water and unprocessed and be directly discharged into urban sewage
Pipeline.Shown according to the testing result to China developed regions such as ground such as Guangzhou, Shanghai food and drink waste water, COD indexs in food and drink waste water
For 1000mg/L or so, far above country《Integrated wastewater discharge standard》(GB8978-1996) emission level specified in, this nothing
Doubt the processing load for adding municipal sewage plant.In addition, the direct discharge of food and drink waste water has an effect on urban drainage pipe network
Discharge capacity, causes body eutrophication etc., serious threat environment and human health.Therefore, the improvement to food and drink waste water becomes
Urgent problem.
At present, the processing for food and drink waste water mainly has bioanalysis (SBR methods, magnetic powder reinforcing activated sludge process, catalytic oxidation
Method, MBR methods), gravity and centrifugal separation, Bubble-floating Method, absorption method, electrochemical process (electrocoagulation, light electrolysis-electrolysis, pulse
Electric flocculation method), the methods of Coagulation Method, but more there are dosing, have the threat of secondary pollution, sludge quantity it is big, it is difficult or
Filler easily blocks, and treatment effect fluctuates the problems such as larger with water quality index such as wastewater pHs.
The content of the invention：
The present invention is directed to shortcoming and defect existing in the prior art, it is proposed that a kind of non-secondary pollution, meal of reasonable cost
Drink waste water treatment and reclamation device and method.
The present invention can be reached by following measures：
A kind of food and drink waste water handles retracting device, it is characterised in that equipped with for separating bulk foreign matter and sewage in waste water
Separate tank, the pulverizer for being crushed to the bulk foreign matter isolated, the biography for foreign matter after crushing to be put into biochemistry pool
Send mechanism, the sedimentation basin for carrying out precipitation filtering to waste water after separation, for carrying out the smelly of oxygenolysis to filtrate after precipitation
Oxygen oxygenation machanism, for after being decomposed to ozone oxidation sewage carry out Air Exposure aeration tank, for being decomposed to biochemistry pool after
Sewage carries out the filtering precipitation mechanism of filtration treatment.
Filling can cut grease and the aerobic microbiological of organic matter in biochemistry pool of the present invention, be equipped with biochemistry pool with
The water distributor that sewage inlet is connected, is additionally provided with jet aerator, sewage (waste water) recirculating pump, microorganism sludge reflux mechanism, in work
During work, the aerator in biochemistry pool pours air into sewage, and circulates water distribution, cloth by sewage (waste water) recirculating pump and water distributor
Hydrophone includes supervisor and with being responsible for the more than two branch pipes being connected, supervisor and the water distribution that flat opening is equipped with branch pipe
Hole, water distributor circulation water distribution can be such that grease in sewage and other organic matters are fully contacted with anaerobe.
The exhaust gear that ozone oxidation mechanism of the present invention includes ozone generator, is connected with ozone generator is smelly
After oxygen is passed into sewage, energy oxygenolysis Organic substance in water is most strong to the oxidability of fiber, alkenes compounds, secondly
Amine and hydrocarbon double bond are thirdly three keys of alkynes for compound, carbocyclic ring heterocyclic compound, sulfide, phosphide etc., ozone pair
The singly-bound oxidability of alcohol, aldehyde, ether and nytron is weaker.Organic matter through ozonization, the increase of its biodegradable；It is smelly
Oxygen can also remove stench in, by bacterial destruction, and neutralizing in the short time, decomposing poison gas.
The multistage filtering grid or more set gradually along waste water stream through direction is equipped with filtering precipitation mechanism of the present invention
Level filter screen, crosses filter cake and is discharged by waste residue elevator, the compound discharge standard of waste water can be discharged directly or as garden
Woods is irrigated.
The invention also provides a kind of food and drink waste water handles recovery method, it is characterised in that comprises the following steps：
Step 1：Food and drink waste water is sent into separate tank, bulk is isolated by filtering grid or filter screen in separate tank
Foreign matter, and bulk foreign matter is sent into pulverizer and is crushed, waste water after filtering is discharged into sedimentation basin；
Step 2：By the waste water after filtering after sedimentation basin precipitates filtering, sewage is aoxidized by ozone oxidation mechanism
Handle, the organic macromolecule material in sewage is broken down into small molecule structure material, and kills except harmful worm's ovum in waste water, carefully
Bacterium, then send waste water into aeration tank；
Step 3：Waste water under the auxiliary through aerator, stops 2-3h, is admitted to biochemistry pool in aeration tank；
Step 4：Aerobic microbiological is filled with biochemistry pool, while the foreign matter in step 1 after crushing is also put into biochemistry pool,
Under the action of sewage (waste water) recirculating pump and water distributor, sewage fully circulates in biochemistry pool, fully anti-with aerobic microbiological
Should, pass through debirs in microbial degradation biochemistry pool；
Step 5：Waste water after biochemistry pool reaction is discharged into filtering precipitation mechanism, and after filtered precipitation, precipitation waste residue can be with
Recycling is used as fertilizer, and filtering gained liquid can be discharged directly or as gardens agricultural irrigation water.
Compared with prior art, the present invention acidic materials or alkaline matter need not be added in sewage disposal process to dirt
Water is adjusted, and does not produce secondary pollution, and waste residue and waste water can recycle after processing, have cost is low, working stability,
The advantages that environment-protection low-consumption.
Brief description of the drawings：
Attached drawing 1 is the structure diagram of the present invention.
Reference numeral：Separate tank 1, pulverizer 2, transport mechanism 3, biochemistry pool 4, sedimentation basin 5, ozone oxidation mechanism 6, aeration
Pond 7, filtering precipitation mechanism 8.
Embodiment：
The present invention is further illustrated below in conjunction with the accompanying drawings.
As shown in Figure 1, the present invention proposes a kind of food and drink waste water processing retracting device, it is characterised in that equipped with for dividing
From the separate tank 1 of bulk foreign matter in waste water and sewage, for the bulk foreign matter isolated is crushed pulverizer 2, be used for
Foreign matter after crushing is put into the transport mechanism 3 of biochemistry pool 4, the sedimentation basin 5 for carrying out precipitation filtering to waste water after separation, is used for
The ozone oxidation mechanism 6 of oxygenolysis is carried out to filtrate after precipitation, is carried out for the sewage after being decomposed to ozone oxidation at aeration
The aeration tank 7 of reason, the filtering for sewage progress filtration treatment after being decomposed to biochemistry pool precipitate mechanism 8.
The interior filling of biochemistry pool 4 of the present invention can cut grease and the aerobic microbiological of organic matter, is equipped with biochemistry pool 4
The water distributor being connected with sewage inlet, is additionally provided with jet aerator, sewage (waste water) recirculating pump, microorganism sludge reflux mechanism,
In the course of work, the aerator in biochemistry pool pours air into sewage, and circulates water distribution by sewage (waste water) recirculating pump and water distributor,
Water distributor includes supervisor and with being responsible for the more than two branch pipes being connected, supervisor and the cloth that flat opening is equipped with branch pipe
Water hole, water distributor circulation water distribution can be such that grease in sewage and other organic matters are fully contacted with anaerobe.
The exhaust gear that ozone oxidation mechanism 6 of the present invention includes ozone generator, is connected with ozone generator is smelly
After oxygen is passed into sewage, energy oxygenolysis Organic substance in water is most strong to the oxidability of fiber, alkenes compounds, secondly
Amine and hydrocarbon double bond are thirdly three keys of alkynes for compound, carbocyclic ring heterocyclic compound, sulfide, phosphide etc., ozone pair
The singly-bound oxidability of alcohol, aldehyde, ether and nytron is weaker.Organic matter through ozonization, the increase of its biodegradable；It is smelly
Oxygen can also remove stench in, by bacterial destruction, and neutralizing in the short time, decomposing poison gas.
The multistage filtering grid or more set gradually along waste water stream through direction is equipped with filtering precipitation mechanism 8 of the present invention
Level filter screen, crosses filter cake and is discharged by waste residue elevator, the compound discharge standard of waste water can be discharged directly or as garden
Woods is irrigated.
The invention also provides a kind of food and drink waste water handles recovery method, it is characterised in that comprises the following steps：
Step 1：Food and drink waste water is sent into separate tank, bulk is isolated by filtering grid or filter screen in separate tank
Foreign matter, and bulk foreign matter is sent into pulverizer and is crushed, waste water after filtering is discharged into sedimentation basin；
Step 2：By the waste water after filtering after sedimentation basin precipitates filtering, sewage is aoxidized by ozone oxidation mechanism
Handle, the organic macromolecule material in sewage is broken down into small molecule structure material, and kills except harmful worm's ovum in waste water, carefully
Bacterium, then send waste water into aeration tank；
Step 3：Waste water under the auxiliary through aerator, stops 2-3h, is admitted to biochemistry pool in aeration tank；
Step 4：Aerobic microbiological is filled with biochemistry pool, while the foreign matter in step 1 after crushing is also put into biochemistry pool,
Under the action of sewage (waste water) recirculating pump and water distributor, sewage fully circulates in biochemistry pool, fully anti-with aerobic microbiological
Should, pass through debirs in microbial degradation biochemistry pool；
Step 5：Waste water after biochemistry pool reaction is discharged into filtering precipitation mechanism, and after filtered precipitation, precipitation waste residue can be with
Recycling is used as fertilizer, and filtering gained liquid can be discharged directly or as gardens agricultural irrigation water.
Compared with prior art, the present invention acidic materials or alkaline matter need not be added in sewage disposal process to dirt
Water is adjusted, and does not produce secondary pollution, and waste residue and waste water can recycle after processing, have cost is low, working stability,
The advantages that environment-protection low-consumption.
Claims (2)
1. a kind of food and drink waste water handles retracting device, it is characterised in that equipped with for separating point of bulk foreign matter and sewage in waste water
Pulverizer from pond, for being crushed to the bulk foreign matter isolated, the transmission for foreign matter after crushing to be put into biochemistry pool
Mechanism, the sedimentation basin for carrying out precipitation filtering to waste water after separation, the ozone for carrying out oxygenolysis to filtrate after precipitation
Oxygenation machanism, carry out for the sewage after being decomposed to ozone oxidation the aeration tank of Air Exposure, for dirty after being decomposed to biochemistry pool
Water carries out the filtering precipitation mechanism of filtration treatment；
Filling can cut grease and the aerobic microbiological of organic matter in the biochemistry pool, be equipped with biochemistry pool and sewage inlet
The water distributor being connected, is additionally provided with jet aerator, sewage (waste water) recirculating pump, microorganism sludge reflux mechanism, during the work time, raw
Change the aerator in pond and air is poured into sewage, and water distribution is circulated by sewage (waste water) recirculating pump and water distributor, water distributor includes master
The water distributing pore of flat opening, water distributor are equipped with pipe and the more than two branch pipes being connected with supervisor, supervisor and branch pipe
Circulation water distribution can be such that grease in sewage and other organic matters are fully contacted with aerobic microbiological；
The multistage filtering grid or multistage filtering sieve set gradually along waste water stream through direction is equipped with the filtering precipitation mechanism,
Cross filter cake to discharge by waste residue elevator, waste water, which meets discharge standard, directly to be discharged or as treegarden irrigation.
2. a kind of food and drink waste water using food and drink waste water as claimed in claim 1 processing retracting device handles recovery method, it is special
Sign is to comprise the following steps：
Step 1：Food and drink waste water is sent into separate tank, it is different by filtering grid or filter screen to isolate bulk in separate tank
Thing, and bulk foreign matter is sent into pulverizer and is crushed, waste water after filtering is discharged into sedimentation basin；
Step 2：By the waste water after filtering after sedimentation basin precipitates filtering, sewage is carried out at oxidation by ozone oxidation mechanism
To manage, the organic macromolecule material in sewage is broken down into small molecule structure material, and kills except harmful worm's ovum in waste water, bacterium,
Then waste water is sent into aeration tank；
Step 3：Waste water under the auxiliary through aerator, stops 2-3h, is admitted to biochemistry pool in aeration tank；
Step 4：Aerobic microbiological is filled with biochemistry pool, while the foreign matter in step 1 after crushing is also put into biochemistry pool, in dirt
Under the action of water-circulating pump and water distributor, sewage fully circulates in biochemistry pool, is fully reacted with aerobic microbiological, leads to
Cross debirs in microbial degradation biochemistry pool；
Step 5：Waste water after biochemistry pool reaction, which is discharged into, filters precipitation mechanism, and after filtered precipitation, precipitation waste residue can recycle
As fertilizer, filtering gained liquid can be discharged directly or as gardens agricultural irrigation water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201511030623.4A CN105481184B (en) | 2015-12-31 | 2015-12-31 | Food and drink waste water handles retracting device and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201511030623.4A CN105481184B (en) | 2015-12-31 | 2015-12-31 | Food and drink waste water handles retracting device and method |
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| Publication Number | Publication Date |
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| CN105481184A CN105481184A (en) | 2016-04-13 |
| CN105481184B true CN105481184B (en) | 2018-05-08 |
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| CN201511030623.4A Active CN105481184B (en) | 2015-12-31 | 2015-12-31 | Food and drink waste water handles retracting device and method |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108911413A (en) * | 2018-08-06 | 2018-11-30 | 邹泽深 | A kind of sewage sludge processing unit |
| CN109485209A (en) * | 2019-01-10 | 2019-03-19 | 立德环保设备制造（广州）有限公司 | A kind of O2The integration apparatus of AO technique food and drink wastewater treatment |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102145967A (en) * | 2011-05-11 | 2011-08-10 | 中山市泰帝科技有限公司 | Device and method for processing restaurant wastewater |
| CN103449667A (en) * | 2013-08-30 | 2013-12-18 | 中国地质大学（武汉） | Method for treating restaurant wastewater by using aerobic microorganism and ozone combined technology |
| CN104193109A (en) * | 2014-09-17 | 2014-12-10 | 安徽省绿巨人环境技术有限公司 | Catering sewage treatment method |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07323297A (en) * | 1994-05-31 | 1995-12-12 | Ebara Jitsugyo Kk | Biological treatment of organic sewage |
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Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102145967A (en) * | 2011-05-11 | 2011-08-10 | 中山市泰帝科技有限公司 | Device and method for processing restaurant wastewater |
| CN103449667A (en) * | 2013-08-30 | 2013-12-18 | 中国地质大学（武汉） | Method for treating restaurant wastewater by using aerobic microorganism and ozone combined technology |
| CN104193109A (en) * | 2014-09-17 | 2014-12-10 | 安徽省绿巨人环境技术有限公司 | Catering sewage treatment method |
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| CN105481184A (en) | 2016-04-13 |
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Address after: 246005 No.80 Tianzhushan Road, Anqing City, Anhui Province Patentee after: Anqing Hulk Environmental Technology Co.,Ltd. Address before: 246005 No.80 Tianzhushan Road, Anqing City, Anhui Province Patentee before: ANHUI GREEN TITAN ENVIRONMENTAL TECHNOLOGY Co.,Ltd. |
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| EE01 | Entry into force of recordation of patent licensing contract |
Application publication date: 20160413 Assignee: Anhui Juren Environmental Technology Co.,Ltd. Assignor: Anqing Hulk Environmental Technology Co.,Ltd. Contract record no.: X2023980035074 Denomination of invention: Catering wastewater treatment and recovery device and method Granted publication date: 20180508 License type: Common License Record date: 20230427 |
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