CN205258174U - Ultrafiltration sewage treatment system - Google Patents
Ultrafiltration sewage treatment system Download PDFInfo
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- CN205258174U CN205258174U CN201520931515.3U CN201520931515U CN205258174U CN 205258174 U CN205258174 U CN 205258174U CN 201520931515 U CN201520931515 U CN 201520931515U CN 205258174 U CN205258174 U CN 205258174U
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Abstract
The utility model discloses an ultrafiltration sewage treatment system, including flocculating reaction pond, sedimentation tank, milipore filter subassembly, gas expose to the sun device, water purification water reservoir device and anti - washing unit, its characterized in that: flocculating reaction pond upper portion is connected raw water intake pipe and can be dropped into the induction pipe of flocculating agent, and flocculating reaction pond pool wall is formed with a recess, the spiral setting of this recess for enabling the rivers formation vortex, flocculating reaction cell -out mouth is connected to the water inlet on sedimentation tank upper portion, and this sedimentation tank inner wall is formed with interval distribution's sediment board, and the delivery port is seted up on sedimentation tank upper portion, and the delivery port is connected in milipore filter subassembly water inlet through ultrafiltration water intake pipe, the milipore filter subassembly include casing, rigid coupling in shells inner wall's ultrafiltration membrane element, connect in the flow sensor of casing outer wall and for the pressor booster pump of intaking of rivers among the ultrafiltration water intake pipe. The utility model discloses simple structure, raw water later carry out the ultrafiltration through flocculation and sediment again to be handled, and the water treatment is effectual, and work efficiency is high, the rivers of back flush can recycle, and the water economy resource improves the water use rate.
Description
Technical field
The utility model belongs to water purification technology field, especially relates to a kind of ultrafiltration sewage processingSystem.
Background technology
In life, people are more and more higher for the requirement of water environment now. Therefore, for sewagePurified treatment be gradually valued by the people. In order to realize for using dirty water purification, occurVarious cleaning system, because the clean-up effect of hyperfiltration treatment system is very remarkable, therefore comesMore factory, workshops etc. bring into use ultrafiltration system to process trade effluent. By to water bodyPressurization is delivered to opposite side by sewage by a side pressure of filtering permeable membrane, the impurity, the bacterium that in water body, existDeng excessive and cannot pass filter membrane due to diameter, be left on water inlet one side, thereby at two of filmSide forms different waters, is dense pool on one side, is clean water area on one side, and realization is clean to sewageChange and process. But, because the dustiness of industrial wastewater is larger, only by this processing of ultrafiltration,Can't remove completely for the refuse existing in the phase, after such water enters the external world, stillEasily water pollutes to external world. And in the long-term process using, the filter of dense pool one sideThe surperficial impurity of film can constantly be piled up, last fouling, thus stop up filter membrane, make waterThe purification of body cannot continue again. Common way is that the water having purified is carried out to backwash to film,The impurity punching of fouling on film is fallen, make water can continue again to filter by film. And quiltFor the water of backwash, together discharge with rushing fallen impurity. But such way pairCaused very large waste in the water of backwash, resource utilization is lower, waste water resource. HaveAlthough a little treatment systems are provided with the water of backwash are reclaimed, for locating of recycle-waterManage perfect not, thereby make recycle-water bring too much impurity into Yuan Shui in mixing with former waterIn, strengthen the workload for the treatment of system, reduce operating efficiency.
Utility model content
The utility model, in order to overcome the deficiencies in the prior art, provides a kind of purified treatment effectGood, backwashing water recoverable, the ultrafiltration sewage treatment system that reclaiming clean degree is high.
To achieve these goals, the utility model by the following technical solutions: a kind of ultrafiltration dirtWater treatment system, comprises flocculation tank, sedimentation basin, hyperfiltration membrane assembly, the gas device, clean that exposes to the sunWater accumulator and back purge system, described flocculation tank top connects former water water inlet pipe and can throwEnter the ingress pipe of flocculant, flocculation tank pool wall is formed with groove, and this groove is for can make currentForm the spirality setting of eddy current, described flocculation tank outlet is connected to entering of sedimentation basin topThe mouth of a river, this sedimentation basin inwall is formed with precipitation plate spaced apart, and water outlet is offered on sedimentation basin topMouthful, delivery port is connected in hyperfiltration membrane assembly water inlet by ultrafiltration inlet pipeline, described milipore filterAssembly comprises housing, be fixed in the milipore filter part of inner walls, be connected in the flow of housing outer wallInductor and be the water inlet booster pump of current pressurization in ultrafiltration inlet pipeline, this water inlet booster pump is establishedOn ultrafiltration inlet pipeline, described housing top offers air inlet, and this air inlet passes through tracheaeBe connected in the gas device that exposes to the sun, described water purification accumulator connects hyperfiltration membrane assembly by water purification outlet pipelineDelivery port, described back purge system is located between hyperfiltration membrane assembly and water purification accumulator, comprises and connectingCounter-flushing pipeline, rushing for current pressurization in counter-flushing pipeline that logical hyperfiltration membrane assembly and water purification holdWash booster pump and control the backwash control valve that counter-flushing pipeline is opened, closed.
Further, also comprise a backwashing water retracting device, comprise described in filtering ponds, connectionThe recovery tube of housing, be connected to the return duct of ultrafiltration inlet pipeline and be placed in the filtration in filtering pondsNet, the upper and lower inwall of filtering ponds all offers stopper slot, dismountable the putting in described screen pack both endsIn described stopper slot, described recovery tube and return duct are equipped with flow control valve.
Further, described ultrafiltration inlet pipeline and water purification outlet pipeline are equipped with Flow-rate adjustmentValve.
Further, the described gas device that exposes to the sun comprises air blast and is located at the intake valve on tracheae.
In sum, the utlity model has following advantage: by former water in flocculation tankEddy motion, can make former water fully react with flocculant, by the impurity flocculation in sewage forLarge particle, by carry out purification place by hyperfiltration membrane assembly to water again after precipitation in sedimentation basinReason, the entirety that improves water purifies purity and purification efficiency, and because oarse-grained impurity is by pre-Filter is tackled, and remaining less impurity slows down at the scale velocity on filter membrane surface, increasesFilter membrane, for the time of water treatment, without often carrying out backwash, reduces the number of times of backwash,Improve purification efficiency. Be provided with backwashing water recovery unit for the water after backwash, to recoilAfter water after washing further purifies, again recycle, improve resource utilization.And the water after backwash refluxes and mixes with former water again through after filtering, and can not cause former waterThe pollution of secondary, can not become the work load for the treatment of system.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
In order to make those skilled in the art person better understand the utility model scheme, will tie belowClose the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is enteredThe description that row is clear, complete.
As shown in Figure 1, a kind of ultrafiltration sewage treatment system, a kind of ultrafiltration sewage treatment system,Comprise flocculation tank 1, sedimentation basin 2, hyperfiltration membrane assembly, gas expose to the sun device, water purification accumulator3 and back purge system. This system be once from front to back flocculation tank 1, sedimentation basin 2,Hyperfiltration membrane assembly, water purification accumulator 3, the described gas device that exposes to the sun is placed in hyperfiltration membrane assembly top, thisIn embodiment, the described gas device that exposes to the sun comprises air blast 10 and is located at the intake valve 61 on tracheae 6,Back purge system is positioned at hyperfiltration membrane assembly below.
Concrete, the left side on described flocculation tank 1 top is connected with a former water water inlet pipe 11,Former water flows in flocculation tank 1 by this pipeline; The right side on flocculation tank 1 top connectsHave an ingress pipe 12, ingress pipe 12 can be put into outside flocculant in flocculation tank 1Mix with former water. The pool wall of flocculation tank 1 is formed with the spiral shell that can make current form eddy currentRevolve connected in star 13, the setting of this groove 13, makes to drop into the former water of legal person and flocculant by topCan contact fully, strengthen flocculating effect. The front side of flocculation tank 1 is sedimentation basin 2,Water inlet is offered on the top of sedimentation basin 2, and water after flocculation is by flocculation tank 1 bottomOutlet flow in sedimentation basin 2; The inwall of this sedimentation basin 2 is formed with precipitation plate spaced apart21, sedimentation basin 2 tops set out the mouth of a river, and delivery port is connected in super by ultrafiltration inlet pipeline 5Filter membrane component water inlet; Water after flocculation is flowed into by sedimentation basin 2 tops, when the precipitation plate byGradually deposition, the Impurity deposition after flocculation is in sedimentation basin 2 bottoms, the comparatively clean water on top byThe delivery port on top flows out, and enters in hyperfiltration membrane assembly.
Further, described hyperfiltration membrane assembly comprises housing 41, is fixedly connected in housing 41The milipore filter part 42 of wall, be connected in the flow inductor 43 of housing 41 outer walls and enter for ultrafiltrationThe water inlet booster pump 44 of current pressurization in water lines 5; This water inlet booster pump 44 is located at ultrafiltration and is enteredIn water lines 5, described housing 41 tops offer air inlet, and this air inlet is by tracheae 6Be connected in the gas device that exposes to the sun, described water purification accumulator 3 connects milipore filter by water purification outlet pipeline 7Assembly delivery port; Described flow inductor 43 arranges corresponding to the position of milipore filter part 42,The monitoring of the flow velocity by the water filtration on milipore filter part 42 flows, can judge ultrafiltrationThe accumulation situation of impurity on film part 42, to carry out backwash to milipore filter part 42 in time.
Concrete, back purge system is located between hyperfiltration membrane assembly and water purification accumulator 3, comprisesBe communicated with hyperfiltration membrane assembly and water purification accumulator 3 counter-flushing pipeline 81, be counter-flushing pipeline 81The recoil that the flushing booster pump 82 of middle current pressurization and control counter-flushing pipeline 81 are opened, closedWash control valve 83. Impurity on milipore filter part 42 is piled up, make milipore filter part 42 forWhen the filtration of water is slowed down, can, by counter-flushing pipeline 81 from the interior water guide of water purification accumulator 3, pass throughAfter rinsing booster pump 82 pressurizations, milipore filter part 42 is carried out to backwash, rush milipore filter partThe impurity of 42 surface sediments.
As preferably, system can also comprise a backwashing water retracting device, to the water of backwashRecycle. Concrete, comprise filtering ponds 91, be communicated in the recovery of described housing 41Manage 92, be connected to the return duct 93 of ultrafiltration inlet pipeline 5 and be placed in the mistake in filtering ponds 91Filter screen 94, after the water of backwash being filtered by screen pack, is passing through return duct 93 timesFlow to ultrafiltration inlet pipeline 5, re-start utilization. For the convenient replacing to screen pack 94,Can on the inwall up and down of filtering ponds 91, offer stopper slot 911, by screen pack 94 both endsBe placed in described stopper slot 911, realize the detachable of screen pack 94.
Further, described recovery tube 92, return duct 93, ultrafiltration inlet pipeline 5 and water purificationOutlet pipeline 7 is provided with flow control valve.
When work, former water enters in flocculation tank 1, and after flocculation, enter sedimentation basin 2 and precipitate,By being drained to hyperfiltration membrane assembly by ultrafiltration inlet pipeline 5, obtain afterwards pure water afterwards,Be stored in water purification accumulator 3; In the process of operation, flow inductor is to milipore filter part42 flow is responded to, in the time that flow velocity is reduced to preset value, and inductor feedback signal, anti-Flusher recoils to milipore filter part 42, the impurity on milipore filter part 42 rushed, itWater after rear backwash is mingled with impurity and together flow in backwash recovery unit, after filtering,Be back in ultrafiltration inlet pipeline 5.
Obviously, described embodiment is only a part of embodiment of the present utility model, and notWhole embodiment. Based on the embodiment in the utility model, those of ordinary skill in the artNot making the every other embodiment obtaining under creative work prerequisite, all should belong toThe scope of the utility model protection.
Claims (4)
1. a ultrafiltration sewage treatment system, comprise flocculation tank (1), sedimentation basin (2),Hyperfiltration membrane assembly, gas expose to the sun device, water purification accumulator (3) and back purge system, itsBe characterised in that: described flocculation tank (1) top connects former water water inlet pipe (11)And can drop into the ingress pipe (12) of flocculant, flocculation tank (1) pool wall formsFluted (13), this groove (13) is that the spirality that can make current form eddy current is establishedPut, described flocculation tank (1) outlet is connected to entering of sedimentation basin (2) topThe mouth of a river, this sedimentation basin (2) inwall is formed with precipitation plate spaced apart (21),Sedimentation basin (2) top sets out the mouth of a river, and delivery port is by ultrafiltration inlet pipeline (5)Be connected in hyperfiltration membrane assembly water inlet, described hyperfiltration membrane assembly comprise housing (41),Be fixed in housing (41) inwall milipore filter part (42), be connected in housing (41)The flow inductor (43) of outer wall and be current pressurization in ultrafiltration inlet pipeline (5)Water inlet booster pump (44), this water inlet booster pump (44) is located at ultrafiltration inlet pipeline(5) upper, described housing (41) top offers air inlet, and this air inlet passes throughTracheae (6) is connected in the gas device that exposes to the sun, and described water purification accumulator (3) passes through water purificationOutlet pipeline (7) connects hyperfiltration membrane assembly delivery port, and described back purge system is located atBetween hyperfiltration membrane assembly and water purification accumulator (3), comprise be communicated with hyperfiltration membrane assembly withThe counter-flushing pipeline (81) of water purification accumulator (3), be counter-flushing pipeline (81)Flushing booster pump (82) and the control counter-flushing pipeline (81) of middle current pressurization are openedThe backwash control valve (83) that opens, closes.
2. ultrafiltration sewage treatment system according to claim 1, is characterized in that: alsoComprise a backwashing water retracting device, comprise filtering ponds (91), be communicated in described shellThe recovery tube (92) of body (41), be connected to the backflow of ultrafiltration inlet pipeline (5)Manage (93) and be placed in the screen pack (94) in filtering ponds (91), filtering ponds (91)Upper and lower inwall all offers stopper slot (911), described screen pack (94) both endsDismountable being placed in described stopper slot (911), described recovery tube (92) and returnStream pipe (93) is equipped with flow control valve.
3. ultrafiltration sewage treatment system according to claim 1, is characterized in that: instituteState ultrafiltration inlet pipeline (5) and water purification outlet pipeline (7) is equipped with Flow-rate adjustmentValve.
4. ultrafiltration sewage treatment system according to claim 1, is characterized in that: instituteStating the gas device that exposes to the sun comprises air blast (10) and is located at the intake valve (61) on tracheae (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520931515.3U CN205258174U (en) | 2015-11-20 | 2015-11-20 | Ultrafiltration sewage treatment system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520931515.3U CN205258174U (en) | 2015-11-20 | 2015-11-20 | Ultrafiltration sewage treatment system |
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| CN205258174U true CN205258174U (en) | 2016-05-25 |
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| CN201520931515.3U Active CN205258174U (en) | 2015-11-20 | 2015-11-20 | Ultrafiltration sewage treatment system |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106731062A (en) * | 2017-01-09 | 2017-05-31 | 珠江水利委员会珠江水利科学研究院 | Pressure filtration formula water purifying device |
| CN109220955A (en) * | 2018-09-04 | 2019-01-18 | 浙江庆渔堂农业科技有限公司 | A kind of ecological cultivation system |
| CN111467964A (en) * | 2020-04-09 | 2020-07-31 | 江苏源泰恒环境工程有限公司 | Sewage treatment ultrafiltration device |
| CN113522028A (en) * | 2021-07-16 | 2021-10-22 | 合肥云雀智能科技有限公司 | Water supply ultrafiltration equipment with remote fault judgment device and fault judgment method |
-
2015
- 2015-11-20 CN CN201520931515.3U patent/CN205258174U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106731062A (en) * | 2017-01-09 | 2017-05-31 | 珠江水利委员会珠江水利科学研究院 | Pressure filtration formula water purifying device |
| CN109220955A (en) * | 2018-09-04 | 2019-01-18 | 浙江庆渔堂农业科技有限公司 | A kind of ecological cultivation system |
| CN111467964A (en) * | 2020-04-09 | 2020-07-31 | 江苏源泰恒环境工程有限公司 | Sewage treatment ultrafiltration device |
| CN113522028A (en) * | 2021-07-16 | 2021-10-22 | 合肥云雀智能科技有限公司 | Water supply ultrafiltration equipment with remote fault judgment device and fault judgment method |
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