CN201372235Y - Integrated reclaimed water advanced treating equipment - Google Patents

Integrated reclaimed water advanced treating equipment Download PDF

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Publication number
CN201372235Y
CN201372235Y CN200820157496U CN200820157496U CN201372235Y CN 201372235 Y CN201372235 Y CN 201372235Y CN 200820157496 U CN200820157496 U CN 200820157496U CN 200820157496 U CN200820157496 U CN 200820157496U CN 201372235 Y CN201372235 Y CN 201372235Y
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CN
China
Prior art keywords
water
treatment equipment
integrated
deep treatment
middle water
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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
Application number
CN200820157496U
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Chinese (zh)
Inventor
余志荣
宋力
徐存德
仰礼军
袁杰
宋伟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shanghai Yike Green Engineering Co Ltd
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Shanghai Yike Green Engineering Co Ltd
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Priority to CN200820157496U priority Critical patent/CN201372235Y/en
Application granted granted Critical
Publication of CN201372235Y publication Critical patent/CN201372235Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses integrated reclaimed water advanced treating equipment, which comprises a carbon filter tank, a softening tank and a precision filter, wherein the water inlet of the carbon filter tank is connected with a reclaimed water inlet pipe, and the water outlet of the carbon filter tank is connected with the water inlet of the softening tank through a pipeline; the water outlet of the softening tank is connected with the water inlet of the precision filter through a pipeline, and the water outlet of the precision filter is connected with a reclaimed water outlet pipe. The equipment adopts activated carbon adsorption filtration and high-precision filter element filtration, so that suspended solids SS in the reclaimed water are effectively separated, the content of organic matter such as oil and the like is reduced, and the tendency of cooling water system sedimentation and microbial propagation is greatly reduced; and with a softener, the hardness of calcium in the reclaimed water is greatly reduced, the risk of scale in a cooling water system is basically eliminated, the requirement of the cooling water system for water quality is met, and further a lot of water resources are saved.

Description

Water deep treatment equipment in integrated
Technical field
The utility model relates to a kind of middle water deep treatment equipment, particularly a kind of equipment that the middle water that produces in the automobile production industry is carried out advanced treatment as the cooling system water coolant before.
Background technology
The waste water of automobile production industry mainly comprises trade effluent and plant area's sanitary sewages such as cleaning and degreasing, electrophoresis, phosphatization, becomes middle water after operations such as materialization, biochemistry, the filter of sand charcoal are handled.For full-sized car manufacturing enterprise, the quantity discharged after day treated generally can reach hundreds of tons even more than the kiloton.If only be used to flush the toilet and greening irrigation, then its water consumption is less, and all the other most of water often just directly emit, and have caused the waste of water resources.Therefore, for water saving, consideration as the open central air-conditioning cooling water replenishment of on-site, like this, has just improved the utilization ratio of middle water with unnecessary middle water greatly, has saved water resources.Yet the calcium ion content of water water quality is higher in the automobile production industry, often exceeds 2~4 times in tap water, and the fouling tendency of cooling water system will increase the weight of greatly; In addition, although all indexs of middle water have reached the standard (GB/T 19923-2005) that is applied to water coolant, but contained a small amount of SS (suspended solid), the COD of middle water, oils etc. still can be brought negative impact to cooling water system, promote microbial reproduction and deposition problems.Therefore, need consideration centering water to make further advanced treatment, so that it can satisfy the demand of water coolant to water quality fully.
The utility model content
At above-mentioned technical problem, the utility model provide a kind of incorporate in water deep treatment equipment, the middle water depth that produces in the automobile production industry is handled after, satisfy the demand of cooling water system to water quality.
Embodiment of the present utility model is achieved through the following technical solutions:
Depth of water treatment facility in a kind of, comprise charcoal filter tank, softening jar, accurate filter, the water-in of described charcoal filter tank is connected with middle water water inlet pipe, the water outlet of charcoal filter tank is connected by the water-in of pipeline with softening jar, described softening jar water outlet is connected with the water-in of accurate filter by pipeline, and the water outlet of described accurate filter is connected with middle water rising pipe.
According to above-mentioned principal character, the water outlet of described middle water rising pipe is equipped with ultraviolet germicidal.
According to above-mentioned principal character, filler is a granular carbon in the described charcoal filter tank.
According to above-mentioned principal character, described softening jar of interior filler is sodium ion exchange resin.
According to above-mentioned principal character, time type multiway valve controller is housed on the described charcoal filter tank.
According to above-mentioned principal character, on the described softening jar flow type multiway valve controller is housed.
According to above-mentioned principal character, be equipped with motorized valve on described middle water water inlet pipe and the middle water rising pipe.
According to above-mentioned principal character, described multiway valve controller is connected with PLC with motorized valve.
According to above-mentioned principal character, tensimeter all is equipped with at the water-in of described accurate filter and water outlet place.
Technique scheme has following beneficial effect: adopt charcoal absorption filtration, high precision filter element filtering in this equipment, make the ss suspended solid in the water obtain effective separation, and reduced organic content such as oils, greatly reduce the tendency of cooling water system deposition and microbial reproduction; Adopted softening agent make in the calcium hardness of water reduce greatly, basically eliminate the fouling risk of cooling water system, satisfied the demand of cooling water system, and then can save great amount of water resources water quality.
Description of drawings
Fig. 1 is the structural representation of the middle water deep treatment equipment that provides of the utility model.
Embodiment
Below in conjunction with accompanying drawing, embodiment is described in detail to the utility model:
As an embodiment of the present utility model, water deep treatment equipment comprises charcoal filter tank 1, softening jar 3 and accurate filter 6 in this.In the charcoal filter tank 1 granular carbon is housed, the water-in of charcoal filter tank 1 is connected with middle supply mains by middle water water inlet pipe, and water pressure gauge P1 and magnetic valve M1 are housed on the middle water water inlet pipe, and the water outlet of charcoal filter tank 1 is connected by the water-in of pipeline with softening jar 3; Charcoal filter tank 1 is furnished with time type multiway valve controller, can realize full automatic backwash function, and the water outlet of charcoal filter tank 1 also is connected with one and flushes out water pipe 2, as being gac back flushing water outlet.Filler in softening jar 3 is a sodium ion exchange resin, and softening jar 3 water-in also is connected with a salt tank 5, is used to deposit the resin regeneration sodium chloride solution, and softening jar 3 water outlet is connected by the water-in of pipeline with accurate filter 5; The softening jar 3 multiway valve controller of being furnished with the flow type can be realized full-automatic backwash, regeneration, the function of just washing, and softening jar 3 water outlet also is connected with one and flushes out water pipe 4, as flushing out the mouth of a river before and after the resin regeneration.In the accurate filter 5 fabric filter element is housed, a tensimeter P2, P3 respectively are equipped with in the water-in of accurate filter 5 and water outlet place, after accurate filter 5 uses for some time, along with the trapped substance on the fabric filter element is cumulative, its top hole pressure can progressively descend, because its intake pressure is constant, so pressure reduction will progressively increase, and filtration efficiency also will be more and more lower.Therefore should often pay close attention to the reading of strainer pressure at both sides table P2, P3 in using, general pressure reduction needs less than certain numerical value, otherwise should consider to change or clean filter core.Water was after ultraviolet germicidal 7 carries out germicidal treatment during the accurate filter water outlet was effusive, and the water rising pipe flows into the cooling basin in the warp, and under meter F and magnetic valve M2 are housed on the middle water rising pipe.One tap water supply pipe also is housed in the cooling basin, magnetic valve M3 is housed on the running water pipe, water supplies water when not enough in realizing, the function of being carried out moisturizing by tap water.Magnetic valve, multiway valve controllers all in this equipment all are connected with the electric control box 8 that PLC is housed, and have realized fully automatic operation, have reduced human cost, have improved safety in operation.
When using this equipment, the middle former water of water is flowed in the charcoal filter tank 1 by middle supply mains, behind organism such as charcoal filter tank 1 absorption oils and the filtering part SS, enter softening jar 3 and carry out ion exchange reaction, remove most calcium ion, remove residual SS through accurate filter 6 again, water outlet can be satisfied cooling system to requirements in water quality after ultraviolet germicidal is made germicidal treatment, enter the water coolant pond at last.Adopt charcoal absorption filtration, high precision filter element filtering in this equipment, the ss suspended solid in making in the water has obtained effective separation, and has reduced organic content such as oils, greatly reduces the tendency of cooling water system deposition and microbial reproduction; Adopted softening agent make in the calcium hardness of water reduce greatly, basically eliminate the fouling risk of cooling water system, satisfied the demand of cooling water system, and then can save great amount of water resources water quality.
Technique scheme just to the explanation of the utility model embodiment, should not be construed as restriction of the present utility model, and any change that all those skilled in the art make according to thought of the present utility model is all within the novel protection domain of this reality.

Claims (9)

  1. One kind integrated in depth of water treatment facility in the water deep treatment equipment, it is characterized in that: this equipment comprises charcoal filter tank, softening jar, accurate filter, the water-in of described charcoal filter tank is connected with middle water water inlet pipe, the water outlet of charcoal filter tank is connected by the water-in of pipeline with softening jar, described softening jar water outlet is connected with the water-in of accurate filter by pipeline, and the water outlet of described accurate filter is connected with middle water rising pipe.
  2. 2. as claim 1 described integrated middle water deep treatment equipment is arranged, it is characterized in that the water outlet of described middle water rising pipe is equipped with ultraviolet germicidal.
  3. 3. integrated middle water deep treatment equipment as claimed in claim 2 is characterized in that filler is a granular carbon in the described charcoal filter tank.
  4. 4. integrated middle water deep treatment equipment as claimed in claim 3 is characterized in that filler is a sodium ion exchange resin in described softening jar.
  5. 5. integrated middle water deep treatment equipment as claimed in claim 4 is characterized in that being equipped with on the described charcoal filter tank time type multiway valve controller.
  6. 6. integrated middle water deep treatment equipment as claimed in claim 5 is characterized in that on described softening jar flow type multiway valve controller being housed.
  7. 7. integrated middle water deep treatment equipment as claimed in claim 6 is characterized in that being equipped with motorized valve on described middle water water inlet pipe and the middle water rising pipe.
  8. 8. integrated middle water deep treatment equipment as claimed in claim 7 is characterized in that described multiway valve controller is connected with PLC with motorized valve.
  9. 9. as claimed in claim 8 integrated in water deep treatment equipment, it is characterized in that the water-in of described accurate filter and water outlet place all be equipped with tensimeter.
CN200820157496U 2008-12-19 2008-12-19 Integrated reclaimed water advanced treating equipment Expired - Fee Related CN201372235Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN200820157496U CN201372235Y (en) 2008-12-19 2008-12-19 Integrated reclaimed water advanced treating equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN200820157496U CN201372235Y (en) 2008-12-19 2008-12-19 Integrated reclaimed water advanced treating equipment

Publications (1)

Publication Number Publication Date
CN201372235Y true CN201372235Y (en) 2009-12-30

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN200820157496U Expired - Fee Related CN201372235Y (en) 2008-12-19 2008-12-19 Integrated reclaimed water advanced treating equipment

Country Status (1)

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CN (1) CN201372235Y (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102320696A (en) * 2011-05-17 2012-01-18 华英伦水科技(宁波)有限公司 Large water treatment equipment and control method thereof
CN102873644A (en) * 2012-10-26 2013-01-16 浙江金汇钢业股份有限公司 Steel surface rust removing device
CN105016542A (en) * 2014-04-28 2015-11-04 宜兴市环球水处理设备有限公司 Packaging bottle washing water recycling method
CN106746073A (en) * 2016-12-08 2017-05-31 苏州陈恒织造有限公司 A kind of water-saving Central water purification processing system and method
CN106746072A (en) * 2016-12-08 2017-05-31 苏州陈恒织造有限公司 A kind of combined type treatment method for rural sewage

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102320696A (en) * 2011-05-17 2012-01-18 华英伦水科技(宁波)有限公司 Large water treatment equipment and control method thereof
CN102873644A (en) * 2012-10-26 2013-01-16 浙江金汇钢业股份有限公司 Steel surface rust removing device
CN102873644B (en) * 2012-10-26 2014-08-27 浙江金汇钢业股份有限公司 Steel surface rust removing device
CN105016542A (en) * 2014-04-28 2015-11-04 宜兴市环球水处理设备有限公司 Packaging bottle washing water recycling method
CN106746073A (en) * 2016-12-08 2017-05-31 苏州陈恒织造有限公司 A kind of water-saving Central water purification processing system and method
CN106746072A (en) * 2016-12-08 2017-05-31 苏州陈恒织造有限公司 A kind of combined type treatment method for rural sewage

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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: 20091230

Termination date: 20161219