CN201914996U - Papermaking waste water treatment device - Google Patents
Papermaking waste water treatment device Download PDFInfo
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- CN201914996U CN201914996U CN2011200084314U CN201120008431U CN201914996U CN 201914996 U CN201914996 U CN 201914996U CN 2011200084314 U CN2011200084314 U CN 2011200084314U CN 201120008431 U CN201120008431 U CN 201120008431U CN 201914996 U CN201914996 U CN 201914996U
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- biological filter
- treatment device
- wastewater treatment
- integral biological
- tank
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- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model relates to a papermaking waste water treatment device which has the main structure of comprising an adjusting tank, a filtering device and a recycling water tank; the device also comprises an integral biological filter group, a clean water pond, a sludge storage tank and an ultraviolet sterilizer; the adjusting tank, the integral biological filter group, the clean water pond, the filtering device, the ultraviolet sterilizer and the recycling water tank are sequentially communicated with one another by lifting pumps and valves; and the adjusting tank, the integral biological filter group and the filtering device are respectively communicated with the sludge storage tank by the valves. The papermaking waste water treatment device has the characteristics that the white waste water treatment capability is strong, the treatment effect is good, the recovered stock is high in quality, the sludge in equipment can be automatically cleaned, and the sludge can be treated in a centralized way.
Description
Technical field
The utility model relates to a kind of waste disposal plant, particularly a kind of papermaking wastewater treatment device.
Background technology
The plain boiled water wastewater treatment method that produces in existing the paper waste treatment process, particularly paper-making process has the combination of coagulate gas floating process, oxidation pond technology, biological aerated filter process etc. or these methods; The technology that a kind of paper mill effluent is handled reuse is disclosed as Chinese patent application numbers 200810038176.0, adopt the super efficiency shallow air flotation method and carry out fibrous bundle or the technology of biological membrane processing, this technology is applicable to the wastewater treatment of package paper, cultural paper, extraordinary paper plant, but when being used to handle the waste water of high-grade slim paper plant such as toilet paper, it reclaims to be easy to generate when slurry utilizes again and disperses inhomogeneous and influence phenomenon such as paper strength.
So be badly in need of at present a kind ofly handling that plain boiled water wastewater treatment ability is strong, treatment effect good, reclaiming the high papermaking wastewater treatment device of stock quality.
The utility model content
Technical problem to be solved in the utility model is that reusable edible, slurry rate of recovery shortcomings such as stock quality difference low, that reclaim do not design a kind of papermaking wastewater treatment device for waste water that present employed papermaking wastewater treatment device exists.
The utility model is achieved through the following technical solutions above-mentioned purpose:
Technical disadvantages at existing papermaking wastewater treatment device exists designs a kind of papermaking wastewater treatment device, and its primary structure comprises equalizing tank, filtration unit and reuse pool.Described device also comprises integral biological filter tank group, clean water basin, storage basin and uv steriliser; Between described equalizing tank, integral biological filter tank group, clean water basin, filtration unit, ultraviolet disinfector and the reuse pool by lift pump and valve UNICOM successively; Equalizing tank, integral biological filter tank group and filtration unit are respectively by valve and storage basin UNICOM.
Be provided with the clorox sterilizing unit between described ultraviolet disinfector and the reuse pool.
Be provided with the coagulating agent adding set between described clean water basin and the filtration unit.
Described clean water basin are by backwash pump while and integral biological filter tank group and filtration unit UNICOM.
Described filtration unit is composed in series by fiber bundle filter and activated charcoal filter.
Described integral biological filter tank group is composed in parallel by two or more integral biological filter tanks; Described integral biological filter tank is composed in series by anoxic biological filter and BAF.
Be provided with lift pump between described storage basin and the equalizing tank.
Be divided into sewage disposal flow process and cleaning process during the work of this device.When carrying out the sewage disposal flow process, effusive plain boiled water waste water is delivered in the equalizing tank from the production unit, and the effective pond of equalizing tank holds 1000m
3, sewage hydraulic retention 5 hours in equalizing tank.The equalizing tank water outlet is promoted in the group of integral biological filter tank by pump then, and integral biological filter tank group is made up of 8 integral biological filter tanks, and effective pond, single integral biological filter tank holds 144m
3Sewage hydraulic retention 6 hours in the group of integral biological filter tank.Sewage is transferred in the clean water basin, the effective pond of clean water basin holds 480m again
3, sewage 2.4 hours laggard line samplings of hydraulic retention in clean water basin detect.Detected result reaches emission standard then can discharge, and discharges not up to standardly then sewage to be delivered to reuse pool.Adding clorox in this process carries out disinfection, filter by fiber bundle filter and activated charcoal filter then, carry out sterilization through ultraviolet disinfector again, arrive reuse pool at last, hydraulic retention can assign production unit to use after 4.5 hours in reuse pool.50 tons/hour of fiber bundle filter single device processing poweies.If 50 tons/hour of activated charcoal filter processing poweies.50 tons/hour of uv steriliser processing poweies;
This device puts into production to be needed to clean after for some time, cleaning process is as follows: at first allow clean water basin fill with water, call retaining in the clean water basin by the backwash water pump, respectively integral biological filter tank group, fiber bundle filter and activated charcoal filter are washed by the backwash water pump, mud in integral biological filter tank group, fiber bundle filter and the activated charcoal filter delivered in the storage basin precipitate, the supernatant liquid of storage basin is sent back in the equalizing tank.Putting aside when the mud in the storage basin just can be with sludge dewatering treatment when a certain amount of.
The utlity model has that plain boiled water wastewater treatment ability is strong, treatment effect good, reclaim the stock quality height and can automatic cleaning equipment in mud, the characteristics that mud can be focused on simultaneously.
Description of drawings
Fig. 1 is the structural representation of the utility model embodiment one;
Fig. 2 is the utility model filter apparatus configuration synoptic diagram;
Fig. 3 is the utility model integral biological filter tank structural representation;
Fig. 4 is the utility model integral biological filter tank group structural representation;
Fig. 5 is the structural representation of the utility model embodiment one sewage disposal state;
Fig. 6 is the structural representation of the utility model embodiment one cleaning equipment state.
Embodiment
Embodiment one: as shown in Figure 1, the primary structure of present embodiment comprises equalizing tank, filtration unit and reuse pool.Described device also comprises integral biological filter tank group, clean water basin, storage basin and uv steriliser; Between described equalizing tank, integral biological filter tank group, clean water basin, filtration unit, ultraviolet disinfector and the reuse pool by lift pump and valve UNICOM successively.More specifically say so at equalizing tank, integral biological filter tank group, clean water basin, filtration unit, ultraviolet disinfector and these devices of reuse pool, all be provided with valve 1 and lift pump 2 between per two devices.Equalizing tank, integral biological filter tank group and filtration unit are respectively by valve 1 and storage basin UNICOM.
As shown in Figure 1, be provided with the clorox sterilizing unit between described ultraviolet disinfector and the reuse pool.Be provided with the coagulating agent adding set between described clean water basin and the filtration unit.
As shown in Figure 1, described clean water basin by wash water pump in anti-7 3 simultaneously and integral biological filter tank group and filtration unit UNICOM.
As shown in Figure 2, described filtration unit is composed in series by fiber bundle filter and activated charcoal filter.
As shown in Figure 4, described integral biological filter tank group is composed in parallel by 8 integral biological filter tanks; As shown in Figure 3, described integral biological filter tank is composed in series by anoxic biological filter and BAF.
Be provided with lift pump 2 between described storage basin and the equalizing tank.
Be divided into sewage disposal flow process and cleaning process during the work of this device.As shown in Figure 5, when carrying out the sewage disposal flow process, effusive plain boiled water waste water is delivered in the equalizing tank from the production unit, and hydraulic retention is 5 hours in equalizing tank.The equalizing tank water outlet promotes 2 to the group of integral biological filter tank by pump then, and hydraulic retention is 6 hours in the group of integral biological filter tank.Sewage is transferred in the clean water basin, hydraulic retention discharged after 2.4 hours in clean water basin again.If desired waste water reclamation is done water of productive use, the waste water that then needs to finish dealing with in clean water basin is transferred to reuse pool, in this process, add coagulating agent by the coagulating agent adding set earlier, filter by fiber bundle filter and activated charcoal filter then, again through ultraviolet disinfector and add clorox and carry out sterilization, arrive reuse pool at last, hydraulic retention can assign production unit to use after 4.5 hours in reuse pool.
As shown in Figure 6, this device puts into production to be needed to clean after for some time, cleaning process is as follows: at first allow clean water basin fill with water, call retaining in the clean water basin by backwash water pump 3, respectively integral biological filter tank group, fiber bundle filter and activated charcoal filter are washed by backwash water pump and backwash blower fan, mud in integral biological filter tank group, fiber bundle filter and the activated charcoal filter delivered in the storage basin precipitate, the supernatant liquid of storage basin is sent back in the equalizing tank.Putting aside when the mud in the storage basin just can be with sludge dewatering treatment when a certain amount of.
Do not pass through the water inlet before the sewage disposal of the present utility model: COD<200mg/L, SS<60mg/L, T≤35 ℃, PH 7-9.Discharging water outlet after treatment can reach: COD≤60mg/L, SS≤30mg/L.Satisfy the demand of paper water fully.
Claims (7)
1. papermaking wastewater treatment device, its primary structure comprises equalizing tank, filtration unit and reuse pool, it is characterized in that described device also comprises integral biological filter tank group, clean water basin, storage basin and uv steriliser; Between described equalizing tank, integral biological filter tank group, clean water basin, filtration unit, ultraviolet disinfector and the reuse pool by lift pump and valve UNICOM successively; Equalizing tank, integral biological filter tank group and filtration unit are respectively by valve and storage basin UNICOM.
2. papermaking wastewater treatment device according to claim 1 is characterized in that being provided with between described ultraviolet disinfector and the reuse pool clorox sterilizing unit.
3. papermaking wastewater treatment device according to claim 2 is characterized in that being provided with between described clean water basin and the filtration unit coagulating agent adding set.
4. papermaking wastewater treatment device according to claim 3 is characterized in that described clean water basin are by backwash pump while and integral biological filter tank group and filtration unit UNICOM.
5. according to claim 1 or 2 or 3 or 4 described papermaking wastewater treatment devices, it is characterized in that described filtration unit is composed in series by fiber bundle filter and activated charcoal filter.
6. papermaking wastewater treatment device according to claim 5 is characterized in that described integral biological filter tank group is composed in parallel by two or more integral biologicals filter tank; Described integral biological filter tank is composed in series by anoxic biological filter and BAF.
7. papermaking wastewater treatment device according to claim 6 is characterized in that being provided with lift pump between described storage basin and the equalizing tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011200084314U CN201914996U (en) | 2011-01-11 | 2011-01-11 | Papermaking waste water treatment device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011200084314U CN201914996U (en) | 2011-01-11 | 2011-01-11 | Papermaking waste water treatment device |
Publications (1)
Publication Number | Publication Date |
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CN201914996U true CN201914996U (en) | 2011-08-03 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN2011200084314U Expired - Fee Related CN201914996U (en) | 2011-01-11 | 2011-01-11 | Papermaking waste water treatment device |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102515411A (en) * | 2011-11-29 | 2012-06-27 | 西安翔德生物科技有限公司 | Biological sewage treatment system |
CN108589391A (en) * | 2018-04-17 | 2018-09-28 | 欧阳克军 | A kind of novel papermaking apparatus that water is removed for paper |
CN109279731A (en) * | 2017-07-19 | 2019-01-29 | 中化化工科学技术研究总院 | A kind of combination sterilizing unit with sustained release, long-acting |
CN111018263A (en) * | 2019-12-30 | 2020-04-17 | 中电环保股份有限公司 | Interface cutting biological purification sewage treatment device |
-
2011
- 2011-01-11 CN CN2011200084314U patent/CN201914996U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102515411A (en) * | 2011-11-29 | 2012-06-27 | 西安翔德生物科技有限公司 | Biological sewage treatment system |
CN109279731A (en) * | 2017-07-19 | 2019-01-29 | 中化化工科学技术研究总院 | A kind of combination sterilizing unit with sustained release, long-acting |
CN108589391A (en) * | 2018-04-17 | 2018-09-28 | 欧阳克军 | A kind of novel papermaking apparatus that water is removed for paper |
CN111018263A (en) * | 2019-12-30 | 2020-04-17 | 中电环保股份有限公司 | Interface cutting biological purification sewage treatment device |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110803 Termination date: 20140111 |