CN2217013Y - High efficiency apparatus for treating high turbidity waste water - Google Patents

High efficiency apparatus for treating high turbidity waste water Download PDF

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Publication number
CN2217013Y
CN2217013Y CN 95207897 CN95207897U CN2217013Y CN 2217013 Y CN2217013 Y CN 2217013Y CN 95207897 CN95207897 CN 95207897 CN 95207897 U CN95207897 U CN 95207897U CN 2217013 Y CN2217013 Y CN 2217013Y
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China
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utility
water
model
industry
sewage
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Expired - Fee Related
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CN 95207897
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Chinese (zh)
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杨昌力
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Individual
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Individual
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Abstract

The utility model relates to a high efficiency purifier for high turbidity sewage. The utility model is characterized in that a filtering area (9) is provided with an inverted cone-shaped cylinder body (14), and a soil discharging bucket conical body (16) which is bigger than a bucket opening is arranged at the upper part of a soil discharging bucket (17). In the device, mixture, reaction, suspension, clarification, sedimentation, filter, clear water collection and sludge concentration are integrated as a whole, and the utility model is a high efficiency purifier for high turbidity sewage and has the advantages of small occupation area, simple and convenient operation and low running cost and has the advantages that the comprehensive technical performance can reach the ideal effect. The utility model is particularly suitable for a granite centrifugal dust remover for a boiler, coal mine sewage, casting industry, ceramics industry, paper making industry, metallurgy industry, chemical industry and the application of the waste water of water milling marble, wet dedusting, etc., to realize the closed cycle of industrial water, and rare raw materials can be recovered.

Description

A kind of efficient high-turbidity sewage cleaner
The utility model belongs to the environmental protection equipment effluent treatment plant.
In the age of current develop rapidly, environmental pollution has become the significant obstacle of human survival and development, especially rationally the quoting and redeveloping of water resources, and the effect that sewage purification device played has obtained people's common attention and care.But it is not high that existing sewage purification device all exists influent turbidity to some extent, water production rate is little, and efficient is low, a series of problems such as operational management and maintenance trouble, its technical process, aspects such as quality of purifying waste water and comprehensive technical performance also remain further to be improved and improve.
The purpose of this utility model be to provide a kind of with mixing, reaction, suspension clarification, precipitation, filtration, clear water compiles and mud simmer down to one, has the effluent treatment plant that can handle high turbidity.Has the purification efficiency height, the ideal effect that technical process is short.
The utility model sewage purification device is according to chemical coagulation, filtering under pressure and hydraulic principle design.This device is made up of institutes such as retort (1), main cylinder (15), spoil disposal bucket (17) and pipe arrangements.The principle of work of this device is: the fs, characteristics according to coagulation process, requirement sewage and coagulating agent uniform mixing, is arranged on the sump pump suction inlet place that draw sewage with dosing mouth with utmost dispatch, utilizes the water pump impeller of high speed rotating can play good stirring action.Sewage at first enters retort (1) and carry out contact reacts with porcelain ball layer (2) in reaction zone (3), tangentially enters in the inner barrel (20) through water folding pipe (4) then, and the sewage that is in turbulent state begins rotation and plays stirring action.
Subordinate phase suspension zone (6) is the zone that alumen ustum forms and grows up gradually, and structure design herein is the taper inner barrel (18) that flow velocity slows down gradually, requires to slow down stirring velocity gradually, in order to avoid the bulk alumen ustum is smashed.
Phase III is settling section (7), and tank body sectional area maximum makes the flow velocity that makes progress the slowest herein, is beneficial to alumen ustum in this sedimentation.
The tetravalence section is filtrating area (9), adopts the poly-third vinyl plastics pearl as filtrate (13) water after the clarification further to be purified again through media filtration.In order to increase the relative velocity of flow of filtering layer, make and form the pressure reduction increase that bypass refluxes, improve the separating power that mud enters mud concentration compartments (5) simultaneously main cylinder (15) top filtrating area (9) is located to be made as back taper cylindrical shell (14), the sectional area that makes filtrating area (9) purifies the big fireballing effect of the water yield gradually less than the sectional area of main cylinder (15) so that reach.Constantly the current that rise enter catchment area (12) through filter head plate (10), directly send clear water to go into water tower or supply user by rising pipe (11) then.
The utility model also is provided with mud concentration compartments (5) and forces effluent recycling pipe (8), and the settled mud in cohesion back is concentrated to the tank body center, through spoil disposal bucket (17), enters mud concentration compartments (5) sedimentation by radiator tube (19).In order to improve amount and the speed that mud enters spoil disposal bucket (17), the top of spoil disposal bucket (17) is made as spoil disposal bucket cone (16) greater than bung, strengthened spoil disposal bucket area suitable for reading like this, slowed down the speed that suspension zone (6) mud rises.According to the filtered water mechanics principle, filtrating area (9) adopts the poly-third vinylic foam pearl to constitute filter bed and flow rate of water flow, under this flow rate regime, force below effluent recycling pipe (8) the level part, filtrate head loss calculated value is greater than 6.6 meter water columns, and force the drag losses calculated value in the effluent recycling pipe (8) only is 0.5 meter water column, by the formed pressure reduction of both pressure differences, having formed jar intravital bypass flows, be that alumen ustum constantly enters mud concentration compartments (5), the more clear water in top, concentration compartments (5) is pressed into automatically forces effluent recycling pipe (8), enters in the filtrating area (9), becomes clear water through the filtration of first half filtrating area and enters catchment area (12).And settled mud is concentrated in the concentration compartments, has prolonged sludge discharging period, has promptly reduced the water ratio of mud, has increased total water production rate again relatively.When reaching certain sludge concentration and after the work period, opening annular shore pipe outlet (22), discharge the mud in the annular shore pipe (21).
The back flushing of filtrate (13) is generally shut down after 8 hours when work, opens recoil pump, and recoil water is entered by rising pipe (11), opens the sewage after recoil blow-off pipe (23) is discharged flushing after flushing finishes.
The retort design is outside main cylinder (15) in addition, and the knot that can increase water and medicament like this touches the time, and also helps maintaining.The primary features of this device is: current tangentially enter formation " point unit vortex " with certain angle and flow, and form, grow up the stage at alumen ustum, spiral motion, the chance that has increased collision between particulate, absorption greatly and condensed makes coagulation more fill part.Main is that after entering settling section, speed of rotation reduces, promptly " circulation strength " is controlled at a threshold value when following, the centrifugal force that alumen ustum obtained is less, according to " point unit vortex " flow principles, and the tank body center of radius minimum, the speed maximum, pressure is then less, and radially under the inside and outside differential pressure effect, alumen ustum is concentrated to the tank body center rapidly at tank body, and enter the spoil disposal bucket, thereby improved the separating effect of alumen ustum (mud) significantly with water.
The utility model is a kind of refining plant of high-turbidity sewage efficiently, and its floor space is little, operates tube just, and working cost is low, and comprehensive technical performance all can reach ideal effect.Can realize the process water closed cycle, and recyclable precious raw material.Especially be fit to boiler granite duster, coal mine sewage, casting, pottery, papermaking, metallurgy, chemical industry every profession and trade, and the application of waste water such as water mill marble, wet dedusting.To the control environmental pollution, water saving all has remarkable social benefit and economic benefit.
The Figure of description brief description:
Accompanying drawing is the diagrammatic cross-section of efficient high-turbidity sewage cleaner.
Among the figure: (1) retort, (2) porcelain ball layer, (3) reaction zone, (4) water inlet folding pipe, (5) mud concentration compartments, (6) suspension zone, (7) settling section, (8) force the effluent recycling pipe, (9) filtrating area, (10) filter head plate, (11) rising pipe, (12) catchment area, (13) filtrate, (14) back taper cylindrical shell, (15) main cylinder, (16) spoil disposal bucket cone, (17) spoil disposal bucket, (18) taper inner barrel, (19) spoke barrel, (20) inner barrel, (21) annular shore pipe, (22) annular shore pipe outlet, (23) recoil blow-off pipe.
The utility model is designed to influent turbidity 5000-15000 mg/litre, and separate unit is per hour handled the water yield 10-250 cubic metres all kinds of models.Can adopt the main cylinder diameter to be 1.4-3.5 meters, the back taper cylindrical shell can be divided into plurality of sections with steel plate and be rolled into circular arc and weld on main cylinder, and its cone angle is general to adopt 60 °.The general employing of spoil disposal bucket cone angle gets final product for 45 °.In addition, the cylindrical shell lower end of filtrating area (9) can be made as the back taper cylindrical shell, also the cylindrical shell of filtrating area (9) all can be made as the back taper cylindrical shell, promptly tapering diminishes.The catchment area height is general to adopt 0.8-1.0 meters.Filtrate adopts directly the poly-third vinylic foam pearl through being 0.8-1.2 millimeters, and thickness of filter bed is generally 0.65 meter.

Claims (3)

1, a kind of efficient high-turbidity sewage cleaner is made up of institutes such as retort (1), main cylinder (15), spoil disposal bucket (17) and pipe arrangements, it is characterized in that: main cylinder (15) top filtrating area (9) locates to be made as back taper cylindrical shell (14), and the top of spoil disposal bucket (17) is made as the spoil disposal bucket cone (16) greater than bung.
2, according to claim 1, described refining plant is characterized in that: the cylindrical shell lower end of filtrating area (9) is made as the back taper cylindrical shell.
3, according to claim 1, described refining plant is characterized in that: the cylindrical shell of filtrating area (9) all is made as the back taper cylindrical shell.
CN 95207897 1995-04-10 1995-04-10 High efficiency apparatus for treating high turbidity waste water Expired - Fee Related CN2217013Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 95207897 CN2217013Y (en) 1995-04-10 1995-04-10 High efficiency apparatus for treating high turbidity waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 95207897 CN2217013Y (en) 1995-04-10 1995-04-10 High efficiency apparatus for treating high turbidity waste water

Publications (1)

Publication Number Publication Date
CN2217013Y true CN2217013Y (en) 1996-01-10

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 95207897 Expired - Fee Related CN2217013Y (en) 1995-04-10 1995-04-10 High efficiency apparatus for treating high turbidity waste water

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CN (1) CN2217013Y (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102633379A (en) * 2012-04-28 2012-08-15 中国矿业大学(北京) Efficient pretreatment system for mine water
CN110255833A (en) * 2019-08-09 2019-09-20 贵州中车绿色环保有限公司 A kind of integrated purifying device handling high concentration, high concentrtion organic wastewater
CN110921883A (en) * 2019-07-15 2020-03-27 廖泰泉 High-concentration sewage deep purification and reuse system and method thereof
CN111170428A (en) * 2019-11-29 2020-05-19 江苏京源环保股份有限公司 High-turbidity wastewater purification method based on movable vehicle-mounted sewage treatment device
CN112390425A (en) * 2020-04-08 2021-02-23 南京帝艾环境科技工程有限公司 Automatic high-concentration sewage purification equipment and working method thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102633379A (en) * 2012-04-28 2012-08-15 中国矿业大学(北京) Efficient pretreatment system for mine water
CN110921883A (en) * 2019-07-15 2020-03-27 廖泰泉 High-concentration sewage deep purification and reuse system and method thereof
CN110255833A (en) * 2019-08-09 2019-09-20 贵州中车绿色环保有限公司 A kind of integrated purifying device handling high concentration, high concentrtion organic wastewater
CN111170428A (en) * 2019-11-29 2020-05-19 江苏京源环保股份有限公司 High-turbidity wastewater purification method based on movable vehicle-mounted sewage treatment device
CN112390425A (en) * 2020-04-08 2021-02-23 南京帝艾环境科技工程有限公司 Automatic high-concentration sewage purification equipment and working method thereof

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C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee