CN102357314A - Full-automatic clearing device - Google Patents

Full-automatic clearing device Download PDF

Info

Publication number
CN102357314A
CN102357314A CN2011102888254A CN201110288825A CN102357314A CN 102357314 A CN102357314 A CN 102357314A CN 2011102888254 A CN2011102888254 A CN 2011102888254A CN 201110288825 A CN201110288825 A CN 201110288825A CN 102357314 A CN102357314 A CN 102357314A
Authority
CN
China
Prior art keywords
clarifier
clearing device
mud
pipe
water inlet
Prior art date
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.)
Pending
Application number
CN2011102888254A
Other languages
Chinese (zh)
Inventor
刘淑杰
方涛
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.)
Heilongjiang Jianlong Iron and Steel Co Ltd
Original Assignee
Heilongjiang Jianlong Iron and Steel Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Heilongjiang Jianlong Iron and Steel Co Ltd filed Critical Heilongjiang Jianlong Iron and Steel Co Ltd
Priority to CN2011102888254A priority Critical patent/CN102357314A/en
Publication of CN102357314A publication Critical patent/CN102357314A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

A full-automatic clearing device relates to a clearing device and resolves the problem in the prior process that the existing clearing device is large in occupied area, inconvenient to manage and high in operation cost. A first clearing device and a second clearing device are arranged in a casing of the clearing device, a water inlet pipe penetrates through the casing of the clearing device to be arranged between the first clearing device and the second clearing device, a first reaction area is formed among the water inlet pipe, the first clearing device and the second clearing device, an inclined pipe bar is arranged on a reversed conical sludge loader which is a sludge area, the inclined pipe bar is a sludge precipitation area, a clear water area is arranged between the above position of the inclined pipe bar and the inner wall of the casing of the clearing device, a water outlet is arranged at the upper end of the outer wall of the casing of the clearing device, a water outlet pipe is arranged on the water outlet, and a first sludge discharging pipe and a second sludge discharging pipe are respectively arranged on the reversed conical sludge loader. The full-automatic clearing device is suitable for being used in turbid circulation water processing equipment.

Description

A kind of full-automatic clarifier
Technical field
The present invention relates to a kind of clarifier, be specifically related to a kind of full-automatic clarifier.
Background technology
The conventional processes of existing traditional metallurgy industry turbid circulating water is: the cooled water of turbid circulating water watering equipment gets into Whirlwind tank and collects and promote with pump; Get into horizontal sedimentation tank, collect pond (hot-tub), pump lifting, high rate filter, cooling tower and water cooling pond; Supply-water pump recycles; But this treatment process exists floor space big, operational management inconvenience, and the high problem of operating cost.
Summary of the invention
The objective of the invention is to exist floor space big in order to solve existing treatment process, operational management inconvenience, and the high problem of operating cost, and then a kind of full-automatic clarifier is provided.
Technical scheme of the present invention is: the full-automatic clarifier of a kind of full-automatic clarifier comprises clarifier housing, water inlet pipe, outlet pipe, first clarifier, second clarifier, first discharge pipeline and second discharge pipeline, first chemical feed pipe, ejector, overflow launder, second charge pipe and Hua Lan filler dress thing; First clarifier and second clarifier are successively set in the clarifier housing from left to right; First chemical feed pipe is arranged on the water inlet pipe; Water inlet pipe passes the clarifier housing and is arranged between first clarifier and second clarifier, forms first reaction zone between the water inlet pipe and first clarifier and second clarifier, and ejector is arranged in first reaction zone; And ejector is connected with water inlet pipe; Second charge pipe and Hua Lan filler dress thing all are arranged in first reaction zone, and first clarifier and second clarifier include mud-sinking area bucket and tipping tube row, and tipping tube row be arranged on the mud-sinking area bucket; The mud-sinking area bucket is the mud district; Tipping tube row is the sludge settling district, is clear water zone between tipping tube row's top and the clarifier inner walls, and delivery port is arranged on the outer wall upper end of clarifier housing; Overflow launder is arranged on the inwall upper end of clarifier housing; And the lower end of overflow launder is higher than delivery port, and outlet pipe is arranged on the delivery port, and outlet pipe is connected with clear water zone; First discharge pipeline and second discharge pipeline are separately positioned on the mud-sinking area bucket of corresponding first clarifier and the second clarifier lower end, and the mud extraction port of first discharge pipeline and second discharge pipeline is arranged on corresponding first mud discharging mouth and the second mud discharging mouth place.
The present invention compared with prior art has following effect: 1. floor space of the present invention is little, and the present invention is 50%~70% of conventional equipment occupation of land, has effectively improved the nervous problem of land used of enterprise.2. the present invention is low from water consumption rate, from water consumption rate approximately: 1%~2%, played positive effect to saving limited water resource.3. construction investment of the present invention is economized, and the present invention is 20%~30% of conventional equipment investment, need not to do the concrete frame structure of a large amount of equipment, water inlet distribution tank, operating platform again, has significantly reduced the civil engineering investment.4. power consumption of the present invention economizes, and installed capacity of the present invention is merely<0.5kw, is 1/10 capacity of miscellaneous equipment, has saved a large amount of power consumption expenses.5. treatment effeciency of the present invention is high, and when water inlet suspension≤15000mg/L, go out aqueous suspension and can guarantee≤10~20mg/L, be that miscellaneous equipment institute is inaccessible.6. operation maintenance of the present invention is convenient, adopts no mechanical form, has reduced fault, only need make regular check on the cleaning inclined tube and get final product.7. spoil disposal moisture content of the present invention is low, and generally speaking, spoil disposal moisture content≤93% is convenient to the dehydration of dehydration equipment, and effectively reduces the time and the cycle of draining.8. automaticity of the present invention is high, owing to adopted the automation mechanized operation operation, influences the treatment effect of equipment so do not receive artificial factor, and cycle, the number of times that only need be directed against the different spoil disposals of adjustment in time of various water quality get final product.
Description of drawings
Fig. 1 is an overall structure sketch map of the present invention; Fig. 2 is the treatment facility (hollow arrow is the flow direction of water, and filled arrows is the flow direction of mud) of turbid circulating water.
The specific embodiment
The specific embodiment one: combine Fig. 1 that this embodiment is described; The full-automatic clarifier of a kind of full-automatic clarifier of this embodiment comprises clarifier housing 1, water inlet pipe 2, outlet pipe 3, first clarifier 4, second clarifier 5, first discharge pipeline 6 and second discharge pipeline 7, first chemical feed pipe 21, ejector 22, overflow launder 23, second charge pipe 24 and Hua Lan filler dress thing 25; First clarifier 4 and second clarifier 5 are successively set in the clarifier housing 1 from left to right; First chemical feed pipe 21 is arranged on the water inlet pipe 2; Water inlet pipe 2 passes clarifier housing 1 and is arranged between first clarifier 4 and second clarifier 5, forms first reaction zone between the water inlet pipe 2 and first clarifier 4 and second clarifier 5, and ejector 22 is arranged in first reaction zone; And ejector 22 is connected with water inlet pipe 2; Second charge pipe 24 all is arranged in first reaction zone with Hua Lan filler dress thing 25, and first clarifier 4 and second clarifier 5 include mud-sinking area bucket 8 and tipping tube row 9, and tipping tube row 9 is arranged on the mud-sinking area bucket 8; Mud-sinking area bucket 8 is the mud district; Tipping tube row 9 is the sludge settling district, is clear water zone between tipping tube row 9 top and clarifier housing 1 inwall, and delivery port 1-1 is arranged on the outer wall upper end of clarifier housing 1; Overflow launder 23 is arranged on the inwall upper end of clarifier housing 1; And the lower end of overflow launder 23 is higher than delivery port 1-1, and outlet pipe 3 is arranged on the delivery port 1-1, and outlet pipe 3 is connected with clear water zone; First discharge pipeline 6 and second discharge pipeline 7 are separately positioned on the mud-sinking area bucket 8 of corresponding first clarifier 4 and second clarifier, 5 lower ends, and the mud extraction port of first discharge pipeline 6 and second discharge pipeline 7 is arranged on the corresponding first mud discharging mouth 1-2 and the second mud discharging mouth 1-3 place.
The specific embodiment two: combine Fig. 1 that this embodiment is described, the blue filler dress thing 25 of spending of this embodiment is the blue filler device of treasure maesa herb.So be provided with, be convenient to the mutual collision of water, increase the water frequency of collision mutually.Other composition is identical with the specific embodiment one with annexation.
In conjunction with Fig. 2 the application of the present invention in the treatment facility of turbid circulating water is described:
Turbid circulating water watering equipment 12 cooled water get in the Whirlwind tank 13; Promote collection through pump, get in the full-automatic clarifier, mud discharging is to the entrance point of sludge treating system 14; Clear water gets in the hot-tub 15; Clear water gets in the cooling tower 17 through promoting the back with muddy water hot-tub elevator pump group 16, enters in the water cooling pond 18 again, recycles through supplying turbid ring apparatus supply-water pump group 19.
Full-automatic clarifier of the present invention has replaced existing horizontal sedimentation tank and two links of high rate filter, saves to take up an area of and the minimizing investment.And operational management is convenient, and operating cost is lower than traditional handicraft.
The present invention is in the treatment process that is applied in the metallurgy industry turbid circulating water time, and the treatment facility of turbid circulating water is to integrate a series of programs such as dispensing, mixing, reaction, one-level separation, cohesion, flocculation, water distribution, current stabilization, deposition, secondary separate, catchment, blowdown, the control of electrical equipment automatic/hand.
The treatment facility of turbid circulating water mainly is successively to carry out hybrid reaction through the sewage that adds flocculating agent, flocculant and need to handle, and with the method through the one-level precipitation separation such as the most of granule foreign in the sewage, dust, suspension, muddy thing, greasy filth, calcium carbonate, sediment is discharged simultaneously; The load of subsequent treatment process and a large amount of reagent consumptions have been alleviated greatly; Remaining fine particle impurity, dust, suspension, muddy thing, greasy filth, calcium carbonate etc. carry out hybrid reaction completely with flocculating agent once more, have increased the probability of mutual collision and absorption, pass through injection well downhole flow regulator and current stabilization district then; Under the effect of current stabilization; Accumulations progressively increases, and most accumulations directly gets into the secondary precipitation separation, and remaining accumulations is in passing through the process of swash plate (pipe); Because the change of angle; Make water and accumulations under different flow rate, obtain separate and subside completely, the accumulations that settles down also gets into the secondary separation and precipitation area simultaneously, through drainage sediment is discharged then.High-quality water after handle on top has really been realized the benign cycle utilization of water quality after collecting through water collector, has brought huge economic benefit to enterprise simultaneously, social benefit and environmental benefit.

Claims (2)

1. full-automatic clarifier; It is characterized in that: full-automatic clarifier comprises clarifier housing (1), water inlet pipe (2), outlet pipe (3), first clarifier (4), second clarifier (5), first discharge pipeline (6) and second discharge pipeline (7), first chemical feed pipe (21), ejector (22), overflow launder (23), second charge pipe (24) and spends blue filler dress thing (25); First clarifier (4) and second clarifier (5) are successively set in the clarifier housing (1) from left to right; First chemical feed pipe (21) is arranged on the water inlet pipe (2); Water inlet pipe (2) passes clarifier housing (1) and is arranged between first clarifier (4) and second clarifier (5); Form first reaction zone between water inlet pipe (2) and first clarifier (4) and second clarifier (5); Ejector (22) is arranged in first reaction zone, and ejector (22) is connected with water inlet pipe (2), second charge pipe (24) and spend blue filler dress thing (25) all to be arranged in first reaction zone; First clarifier (4) and second clarifier (5) include mud-sinking area bucket (8) and tipping tube row (9); Tipping tube row (9) is arranged on the mud-sinking area bucket (8), and mud-sinking area bucket (8) is the mud district, and tipping tube row (9) is the sludge settling district; Between tipping tube row's (9) top and clarifier housing (1) inwall is clear water zone; Delivery port (1-1) is arranged on the outer wall upper end of clarifier housing (1), and overflow launder (23) is arranged on the inwall upper end of clarifier housing (1), and the lower end of overflow launder (23) is higher than delivery port (1-1); Outlet pipe (3) is arranged on the delivery port (1-1); And outlet pipe (3) is connected with clear water zone, and first discharge pipeline (6) and second discharge pipeline (7) are separately positioned on the mud-sinking area bucket (8) of corresponding first clarifier (4) and second clarifier (5) lower end, and the mud extraction port of first discharge pipeline (6) and second discharge pipeline (7) is arranged on corresponding first mud discharging mouth (1-2) and second mud discharging mouth (1-3) is located.
2. according to the said a kind of full-automatic clarifier of claim 1, it is characterized in that: spend blue filler dress thing (25) to be the blue filler device of treasure maesa herb.
CN2011102888254A 2011-09-26 2011-09-26 Full-automatic clearing device Pending CN102357314A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011102888254A CN102357314A (en) 2011-09-26 2011-09-26 Full-automatic clearing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011102888254A CN102357314A (en) 2011-09-26 2011-09-26 Full-automatic clearing device

Publications (1)

Publication Number Publication Date
CN102357314A true CN102357314A (en) 2012-02-22

Family

ID=45582729

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011102888254A Pending CN102357314A (en) 2011-09-26 2011-09-26 Full-automatic clearing device

Country Status (1)

Country Link
CN (1) CN102357314A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3797668A (en) * 1969-07-07 1974-03-19 Pielkenrood Vinitex Bv Separation device
CN201214028Y (en) * 2008-05-15 2009-04-01 宜兴市鑫峰环保设备有限公司 High efficiency sewage precipitator
CN101596374A (en) * 2009-06-23 2009-12-09 中国海洋石油总公司 Swirling flow reaction inclined tube sedimentation tank
CN202237406U (en) * 2011-09-26 2012-05-30 黑龙江建龙钢铁有限公司 Automatic clarificator

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3797668A (en) * 1969-07-07 1974-03-19 Pielkenrood Vinitex Bv Separation device
CN201214028Y (en) * 2008-05-15 2009-04-01 宜兴市鑫峰环保设备有限公司 High efficiency sewage precipitator
CN101596374A (en) * 2009-06-23 2009-12-09 中国海洋石油总公司 Swirling flow reaction inclined tube sedimentation tank
CN202237406U (en) * 2011-09-26 2012-05-30 黑龙江建龙钢铁有限公司 Automatic clarificator

Similar Documents

Publication Publication Date Title
CN203545807U (en) Micro-sand circular settling pond for sewage treatment
CN103232132A (en) Magnetic separation method and apparatus for mine water underground treatment
CN107973515B (en) River course environmental protection desilting and portable sludge thickening dewatering system
CN108101268B (en) Self-sustaining recycling process for treating ballast stone washing wastewater
CN103288243A (en) A system and a method for recycling coal mine drainage and power plant waste water with zero discharge
CN203355383U (en) Coagulative precipitation tank
CN202237406U (en) Automatic clarificator
CN203845894U (en) Laboratory inorganic wastewater treatment device
CN101805108A (en) Device and method for treating sludge underwater
CN101880078B (en) High-efficiency low-consumption complete equipment for coagulation clarification sludge concentration
CN203392959U (en) Device for separating waste catalyst from flue gas desulfurization waste water
CN112794505A (en) Electric furnace short-flow steel plant water treatment and wastewater zero discharge process
CN102826638B (en) Multiphase flow assembly type closed coagulation settling device
CN203540146U (en) Novel efficient physical-chemical water processing and precipitating device
CN202576132U (en) System for closed cyclic utilization of cinder flushing water in sulfuric acid preparation
CN205188014U (en) Wet flue gas desulfurization effluent treatment plant of thermal power plant
CN102357314A (en) Full-automatic clearing device
CN102730890A (en) High-concentration phosphorus-containing and fluorine-containing sewage treatment device
CN202822884U (en) Inclined tube or inclined plate sedimentation tank with sludge concentration function
CN203890153U (en) Complete set of water quality purification treatment all-in-one equipment
CN203545862U (en) Chemical phosphorus removal and precipitation separation device for sludge
CN103641259B (en) Desulfurization wastewater treatment device
CN201485345U (en) Pulp water purification treatment device
CN206538303U (en) The processing system of confluence of rainwater and sewage sewage
CN1765776A (en) Electrolytic aluminium factory production waste water disposal method

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20120222