CN103332806A - Automatic water processing system - Google Patents
Automatic water processing system Download PDFInfo
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- CN103332806A CN103332806A CN2013102505881A CN201310250588A CN103332806A CN 103332806 A CN103332806 A CN 103332806A CN 2013102505881 A CN2013102505881 A CN 2013102505881A CN 201310250588 A CN201310250588 A CN 201310250588A CN 103332806 A CN103332806 A CN 103332806A
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- automatic water
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- processing device
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- treatment system
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Abstract
The invention discloses an automatic water processing system. The automatic water processing system comprises a regulating pool, a lifting pump, an automatic water processing device and a sludge impurity processing device, wherein the regulating pool is connected with the lifting pump, and the lifting pump is connected with a sludge processing device; the automatic water processing device is connected with the sludge impurity processing device, the automatic water processing device comprises a shell and a control cabinet, and the shell is internally divided into a mixing reaction flocculation region and a sediment filtering region from left to right; upper and lower ends of the mixing reaction flocculation region are respectively provided with a water inlet and an air inlet, one side of the top end of the sediment filtering region is provided with a pure water outlet, and the mixing reaction flocculation region and the sediment filtering region are divided by two baffles at intervals; an overflowing channel is formed between the two baffles, an overflowing port is formed between the top end of the left side baffle and the top end of the shell, and a lifting channel is formed between the bottom end of the right side baffle and the bottom end of the shell; the top of the sediment filtering region is provided with an inclined plate packing layer, the bottom end of the sediment filtering region is provided with a plurality of paralleling cone mud collecting hoppers, and the bottom end of the mud collecting hoppers are directly connected with the sludge impurity processing device. The automatic water processing system provided by the invention has the advantages that the process is simple, the processing range is wide, the required equipment is less, the floor space is less, the investment is saved, the manpower is less, the operation and management are convenient, and the operation cost is less.
Description
Technical field
The present invention relates to a kind of water quality clarifying treatment equipment, relate in particular to a kind of water treating equipment of automatization.
Background technology
Existing sewage disposal device on the market generally includes flocculation reaction chamber and filler filtering layer, but its function singleness, treatment effect is undesirable, and need a plurality of equipment to cooperatively interact, floor space is bigger, and processing efficiency is lower, the most important thing is to realize to recycle and control automatically, caused the waste of the energy easily, and energy consumption is higher.
Summary of the invention
The present invention provides a kind of technology simple for solving the problems of the technologies described above, and process range is wide, and required equipment is few, and floor space is little, and reduced investment is artificial few, convenient operation and management, the automatic water treatment system that working cost is low.
The present invention is directed to above-mentioned technical problem, provide following technical scheme: a kind of automatic water treatment system, it is characterized in that comprising equalizing tank, lift pump, waste disposal plant and mud impurity treatment unit, described equalizing tank connects lift pump, lift pump connects waste disposal plant, waste disposal plant connects mud impurity treatment unit, waste disposal plant comprises housing, housing, be divided into hybrid reaction flocculation zone and sedimentation and filtration district in the housing from left to right, described hybrid reaction flocculation zone respectively offers water-in and inlet mouth in two ends up and down, nearly top, described sedimentation and filtration district one side offers pure water inlet, the interval baffle plate with two intervals of described hybrid reaction flocculation zone and sedimentation and filtration separates, constitute overflow ducts between two plate washers, baffle plate top, left side and housing top form overflow port, and plate washer bottom, right side and housing bottom form rising passway, and nearly top, described sedimentation and filtration district is provided with the swash plate packing layer, the bottom is several taper sludge hoppers arranged side by side, and the bucket bottom is communicated with the spoil disposal pipeline.
As preferably, described swash plate packing layer inner swash plate arranges with water inlet direction reversal dip 65 degree.
As preferably, set up a strumbox by the described sedimentation and filtration district, described strumbox upper end is communicated with pure water inlet, built-in filtering layer, the bottom sets out the mouth of a river.
As preferably, set up a PH setter above the described sedimentation and filtration district, the PH setter is communicated with top, sedimentation and filtration district.
As preferably, described housing is the PLC time variable control.By this kind time of time, dose and the flocculation reaction of effective control dosing is set, improves processing efficiency.
As preferably, be that the hybrid reaction flocculation zone offers drug feeding pipeline in addition and connects chemicals dosing plant.
Beneficial effect of the present invention: the invention relates to purification of water quality is handled, the sewage qualified discharge is handled, and the processing unit in the sewage recycling treating processes is optimized innovation, and the equipment that makes it is realized built-up type, the full automatic control operation.It is simple to have technology than prior art, and process range is wide, and required equipment is few, and floor space is little, and reduced investment is artificial few, convenient operation and management, and working cost is low.Not only having saved working cost, and recycled precious water resource, rationally handled the mud impurity in the water, reduced secondary pollution, is the efficient treatment facility that purifies water.
Description of drawings
Fig. 1 is structural representation of the present invention.
Embodiment
A kind of automatic water treatment system, comprise equalizing tank 001, lift pump 002, automatic water softener 003 and mud impurity treatment unit 004, described equalizing tank 001 connects lift pump 002, lift pump 002 connects waste disposal plant 003, waste disposal plant 003 connects mud impurity treatment unit 004, automatic water softener 003 comprises housing 031, housing 032, be divided into mixed flocculation district 311 and sedimentation and filtration district 312 in the housing 031 from left to right, described hybrid reaction flocculation zone respectively offers water-in 311a and inlet mouth 311b in two ends about in the of 311,312 nearly tops, described sedimentation and filtration district, one side offers pure water inlet 312a, 312 baffle plates (313 with two intervals in described hybrid reaction flocculation zone 311 and sedimentation and filtration district, 314) separate, two plate washers (313,314) constitute overflow ducts 315 between, baffle plate 313 tops, left side and housing 031 top form overflow port, right side plate washer 314 bottoms and housing 031 bottom form the rising filtration channel, 312 nearly tops, described sedimentation and filtration district are provided with swash plate packing layer 316, and top is provided with PH and regulates mouth 321.The bottom is several taper sludge hoppers 317 arranged side by side, and bucket 317 bottoms are communicated with spoil disposal pipeline 318.Described swash plate packing layer 316 inner swash plates arrange with water inlet direction reversal dip 65 degree.The described sedimentation and filtration district 312 other strumboxes 319 of setting up, described strumbox 319 upper ends are communicated with pure water inlet 312a, built-in filtering layer, the bottom sets out mouth of a river 319a.
Described sedimentation and filtration district sets up a PH setter 033 in 312 tops, and PH setter 033 is communicated with 312 tops, sedimentation and filtration district.
Described housing is the PLC time variable control.Mixed flocculation district 311 offers drug feeding pipeline in addition and connects chemicals dosing plant 319.
Described mud impurity treatment unit 004 is the treatment facility of prior art routine, for example: filter press, folded sieve formula sludge dewatering equipment etc.
This equipment carries out gravity voluntarily and concentrates by in 312 bottoms, sedimentation and filtration district taper bucket 317 being set, making the mud that precipitates, and needn't be equipped with sludge thickener again, greatly reduces equipment cost.
Below for handling the concrete case that certain copper processing enterprise produces waste water:
Handle the waste water of water inlet for producing in certain copper processing enterprise production process, turbidity 86mg/l, oily 100mg/l, cupric ion 120mg/l, zinc 3.6mg/l, PH=3, water temperature 18 degree.Waste water is opened lift pump 002 automatically when equalizing tank 001 arrives the liquid level of setting, interlock adds gives the medicament of setting earlier, dose, water inlet is entered by the water-in 311a of automatic water softener 003, from inlet mouth 311b it is mixed pressurized air, (preventing sludgd deposition and dead angle), carry out flocculation reaction, sewage after the flocculation reaction enters sedimentation and filtration district 312 through overflow port, up sewage is advanced to filter by swash plate packing layer 316 again, the macrobead of flocculation utilizes gravity settling to arrive in the taper bucket 317 of bottom, discharge by spoil disposal pipeline 318, the water purification of handling enters strumbox 319 by pure water inlet 312a and discharges from water outlet 319a, and it is standby to enter follow-up reuse water spot or reuse pool by pipeline.According to the time of setting (starting shooting back 4 hours), promote mud that spoil disposal pipeline 318 discharges automatically to mud impurity treatment unit 004 by sludge pump, can accumulating through being concentrated to that mud is shaped.Handle back delivery turbidity 5mg/l, oily 7mg/l, copper 0.45mg/l, zinc 0.2mg/l, PH=7.
Opposite high-density inclined tube with water (flow) direction is housed in the described inclined tube packing layer, oblique long 1000mm, inclined tube becomes the hexagonal shape, and Inner footpath 35mm installs rake angle 65 degree, and material is the corrosion-resistant plate of moulding.
Mud impurity after treatment, the thickening moulding can accumulating, through assay, wherein the content of copper reaches 12% in the mud, reaches treatment effect.
Claims (6)
1. automatic water treatment system, it is characterized in that comprising equalizing tank, lift pump, waste disposal plant and mud impurity treatment unit, described equalizing tank connects lift pump, lift pump connects waste disposal plant, automatic water softener connects mud impurity treatment unit, automatic water softener comprises housing, housing, be divided into hybrid reaction flocculation zone and sedimentation and filtration district in the housing from left to right, described hybrid reaction flocculation zone respectively offers water-in and inlet mouth in two ends up and down, nearly top, described sedimentation and filtration district one side offers pure water inlet, the interval baffle plate with two intervals of described hybrid reaction flocculation zone and sedimentation and filtration separates, constitute overflow ducts between two plate washers, baffle plate top, left side and housing top form overflow port, plate washer bottom, right side and housing bottom form rising passway, nearly top, described sedimentation and filtration district is provided with the swash plate packing layer, and the bottom is several taper sludge hoppers arranged side by side, and the bucket bottom is communicated with the spoil disposal pipeline.
2. according to claim 1 described a kind of automatic water treatment system, it is characterized in that described swash plate packing layer inner swash plate and water inlet direction reversal dip 65 degree arrange.
3. according to claim 1 described a kind of automatic water treatment system, it is characterized in that the other strumbox of setting up in described sedimentation and filtration district, described strumbox upper end is communicated with pure water inlet, built-in filtering layer, and the bottom sets out the mouth of a river.
4. according to claim 1 described a kind of automatic water treatment system, it is characterized in that setting up a PH setter above the described sedimentation and filtration district, the PH setter is communicated with top, sedimentation and filtration district.
5. according to claim 1 described a kind of automatic water treatment system, it is characterized in that described housing is the PLC time variable control.
6. according to claim 1 described a kind of automatic water treatment system, it is characterized in that the hybrid reaction flocculation zone offers drug feeding pipeline in addition and connects chemicals dosing plant.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013102505881A CN103332806A (en) | 2013-06-24 | 2013-06-24 | Automatic water processing system |
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| CN2013102505881A CN103332806A (en) | 2013-06-24 | 2013-06-24 | Automatic water processing system |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103837391A (en) * | 2014-03-26 | 2014-06-04 | 马志明 | Water quality monitoring water sample pre-treating device |
| CN103880208A (en) * | 2014-03-05 | 2014-06-25 | 安徽永恒动力科技有限公司 | Plumbic acid wastewater treatment process |
| WO2017070882A1 (en) * | 2015-10-29 | 2017-05-04 | 安尼康（福建）环保设备有限公司 | Flocculation concentration device with grid structural body and filtrate recovery tank |
| CN106915871A (en) * | 2017-03-20 | 2017-07-04 | 环境保护部南京环境科学研究所 | Treated sewage reusing sewage-treatment plant |
| CN107129076A (en) * | 2017-07-06 | 2017-09-05 | 云南省环境科学研究院(中国昆明高原湖泊国际研究中心) | A kind of muddy water tiny flocculation filters device and method soon |
| CN112537830A (en) * | 2020-11-23 | 2021-03-23 | 杭州王之新创信息技术研究有限公司 | Sedimentation bin, environment-friendly water treatment device and environment-friendly aquatic animal feeding device |
| CN115367991A (en) * | 2022-09-01 | 2022-11-22 | 中铁工程服务有限公司 | Horizontal concentrating apparatus and method of use |
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2013
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| JP2002085907A (en) * | 2000-09-14 | 2002-03-26 | Japan Organo Co Ltd | Flocculating and settling apparatus |
| JP2002239481A (en) * | 2001-02-15 | 2002-08-27 | Togami Electric Mfg Co Ltd | Method and apparatus for cleaning wood |
| CN1513773A (en) * | 2003-06-27 | 2004-07-21 | 孙力平 | High effect composite clarifying reaction pond and coagulating, precipitcting water treatment process |
| CN1600695A (en) * | 2004-09-24 | 2005-03-30 | 哈尔滨工业大学 | Air flotation and sedimentation solid-liquid separation device |
| CN201347383Y (en) * | 2009-02-13 | 2009-11-18 | 王中余 | Integrated coal water purifier with high efficiency |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103880208A (en) * | 2014-03-05 | 2014-06-25 | 安徽永恒动力科技有限公司 | Plumbic acid wastewater treatment process |
| CN103880208B (en) * | 2014-03-05 | 2015-09-09 | 安徽永恒动力科技有限公司 | A kind of plumbic acid waste water treatment process |
| CN103837391A (en) * | 2014-03-26 | 2014-06-04 | 马志明 | Water quality monitoring water sample pre-treating device |
| WO2017070882A1 (en) * | 2015-10-29 | 2017-05-04 | 安尼康（福建）环保设备有限公司 | Flocculation concentration device with grid structural body and filtrate recovery tank |
| CN106915871A (en) * | 2017-03-20 | 2017-07-04 | 环境保护部南京环境科学研究所 | Treated sewage reusing sewage-treatment plant |
| CN106915871B (en) * | 2017-03-20 | 2022-03-25 | 环境保护部南京环境科学研究所 | Reclaimed water reuse sewage treatment device |
| CN107129076A (en) * | 2017-07-06 | 2017-09-05 | 云南省环境科学研究院(中国昆明高原湖泊国际研究中心) | A kind of muddy water tiny flocculation filters device and method soon |
| CN112537830A (en) * | 2020-11-23 | 2021-03-23 | 杭州王之新创信息技术研究有限公司 | Sedimentation bin, environment-friendly water treatment device and environment-friendly aquatic animal feeding device |
| CN112537830B (en) * | 2020-11-23 | 2021-11-23 | 湖南苋鲜生态科技有限公司 | Sedimentation bin, environment-friendly water treatment device and environment-friendly aquatic animal feeding device |
| CN115367991A (en) * | 2022-09-01 | 2022-11-22 | 中铁工程服务有限公司 | Horizontal concentrating apparatus and method of use |
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Application publication date: 20131002 |