CN2035651U - Integral high-efficient precipitation and concentration device - Google Patents

Integral high-efficient precipitation and concentration device Download PDF

Info

Publication number
CN2035651U
CN2035651U CN 88213116 CN88213116U CN2035651U CN 2035651 U CN2035651 U CN 2035651U CN 88213116 CN88213116 CN 88213116 CN 88213116 U CN88213116 U CN 88213116U CN 2035651 U CN2035651 U CN 2035651U
Authority
CN
China
Prior art keywords
frid
concentrating unit
guiding tube
type frid
mud
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.)
Withdrawn
Application number
CN 88213116
Other languages
Chinese (zh)
Inventor
赵玉龙
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN 88213116 priority Critical patent/CN2035651U/en
Publication of CN2035651U publication Critical patent/CN2035651U/en
Withdrawn legal-status Critical Current

Links

Images

Abstract

The utility model relates to an integral high-efficient precipitation and concentration device, belonging to the processing equipment of solid-liquid separation for feedwater and sewerage. The utility model is provided with a mixer, a V-shaped groove plate, a forced guiding mud pipe, a forced outlet pipe, a settling chamber and a concentrating chamber. The measures of the V-shaped groove plate and forced soil discharging are used to make the precipitation efficiency enhanced. The problem of difficult soil discharging in a multi-ply sedimentation tank is solved. The utility model can be widely used for any solid-liquid separation of water treatment, in particular for the solid-liquid separation of feedwater or sewage of raw water with high concentration.

Description

Integral high-efficient precipitation and concentration device
The integrated high-efficiency concentrating unit belongs to the solid-liquid separating equipment of feedwater and sewage disposal, can be used for the solid-liquid separation of any water treatment, is specially adapted to the solid-liquid separation of the feedwater or the sewage disposal of the former water of high density.
The solid-liquid separation of existing tap water and sewage disposal, the intermediate processings that adopt wherein have rectangular sedimentation tank and vertical sedimentation basin more, and more advanced swash plate and tube settler are also arranged, they are all low than multi-tiered plate settling tank effect, and have the problem of spoil disposal difficulty.
The purpose of this utility model just provides a kind of dull and stereotyped multilayer settler, and it is than existing like product efficient height, less investment, instant effect.
The utility model is realized in the following manner.
Theory and practice proves, the deposition efficiency of solid-liquid separation: E=(Au 0In the formula of)/(Q), E 2Deposition efficiency (%), Q: flow (m 3/ time), U 0: sedimentation speed (mm/ second), A: desilting area (m 2).Can improve the best approach of deposition efficiency E, strengthen desilting area exactly.The utility model has designed a kind of V-type frid, and takes to force shore pipe, and mud concentrates the measure of grade, has reached and has both improved settling efficiency, solves the difficulty of spoil disposal again.
Be illustrated below in conjunction with an embodiment.
Fig. 1. be integrated high-efficiency precipitation concentrating unit structure iron.
(14) are integrated high-efficiency precipitation concentrating unit pond bodies among the figure, and the pond body has header (7) in the middle of the upper end, is connected with (11) ten layers of eight V-type frids around it, parallel placement, and V-type frid shape is seen Fig. 3.The V-type frid that multilayer is parallel is connected into one, has played the fixed action of an end by in the middle of the frid notch 50-100mm to force mud guiding tube (5) to pass every, and having formed one is the similar Polygons cylinder at center with header (7).The space that it and pond body (14) shell form is distributing water room (3), and the alternate place of adjacent two V-type frids (11) is settling chamber (4), and it communicates with header (7).Force to have into mud hole (13) on the mud guiding tube (5).The pond body is divided into two layers and all is tapered, and the upper strata is reaction chamber (2), and lower floor is mud concentration compartments (6).The spiral type mixing tank (1) of this example can be contained in the middle of the reaction chamber (2), also can be located at externally separately, taps into water pipe (18), and former water enters water inlet pipe (18) back to be mixed in mixing tank.Force outlet pipe (9) to be installed on pond body (14) shell, distributing water room (3) is connected in its upper end, and mud concentration compartments (6) is connected in the lower end, forces rising pipe that control aquifer yield valve (19) is housed.One stabilier (12) is arranged in the mud concentration compartments, be one cylindric, ligation chamber, upper end (2) the awl end,, lower end and concentration compartments (3) are bored the end and are stayed a slit, have limbers (20) on the stabilier, can avoid interference the pressure water outlet.Shore pipe (10) is discharged the mud of concentration compartments.Body top, pond envelope is stayed a space with Chi Gai (15) between the two, with the water vapor bubbles of discharging in the water treatment procedure, suspended substance will concentrate in this zone, and Chi Gai (15) opens at the edge row's bubble pipe (16), in order to drainage water, bubble, suspended substance.Chi Gai (15) adorns a vent valve (17) on the top.
Constituting each component materials of integrated high-efficiency precipitation concentrating unit, can be metallic substance, also can be plastics or glass-reinforced plastic material.
Fig. 2 is an integrated high-efficiency precipitation concentrating unit vertical view.
Fig. 3 is the V-type frid.
The working process of this device:
Former water is from the spiral type mixing tank (1) of water inlet pipe (8) through selecting for use, be mixed into reaction chamber (2), water flow velocity slows down, slowly rise to distributing water room (3), pass through multilayer V-type frid again to the settling chamber (4), sludge settling is on V-type frid (11) in the water, and mud is transported to concentration compartments (6) by forcing the mud hole (13) of advancing on the mud guiding tube (5) to enter pressure mud guiding tube (5).Spissated mud is discharged by shore pipe (10).The mud transfer rate of forcing mud guiding tube is by forcing the valve (19) on the rising pipe (9) to be controlled.Clear water footpath header (7) in the settling chamber (4) is drained by rising pipe (8).
V-type frid optimum size in the utility model design:
Flute length A:300-500mm
The high C:60-100mm of groove
Slot opening B:230-300mm
The spacing that is arranged in parallel of two V-type grooves is 60-100mm
Force the diameter D:25-32mm of mud guiding tube
The economic technology of integrated high-efficiency precipitation concentrating unit and old-fashioned sloping plate deposition is an example to handle water yield 500m/ day relatively:
Device name The residence time (minute) Angle is set Load Treatment effect
Reaction Precipitation Water distribution Amount to Area m 3/M 3Day Molten long-pending m 3/M 3Day Delivery turbidity mg/l Clearance %
The design 2 2 1 5 0 62 350 17-28 93-97
Existing tiltedly (1) board-like (2) 6 10 17 15 4 5 27 30 45 60 141 146.4 137 140 About 20 about 20 793 793
Integrated high-efficiency precipitation concentrating unit, adopted the technical measures of forcing shore pipe, solved the spoil disposal problem of multi-layer planar, adopted pressure spoil disposal and mud to concentrate and also improved the mud concentrated effect, use this device, the total residence time of water is short, is 1/6 of ramp type, the clearance height, the volumetric loading height, volume is little, and cost is low, and the water after the processing easily reaches international emission standard.

Claims (4)

1, a kind of by mixing tank, the V-type frid, force mud guiding tube, force rising pipe, the integrated high-efficiency precipitation concentrating unit that the implict flow plate is formed, it is characterized in that header (7) is positioned in the middle of precipitation concentrating unit pond body (14) upper end, multilayer V-type frid (11) is arranged around it, be connected in series with pressure mud guiding tube (5) in the middle of the every frid notch, the frid the other end and header (7) join, form similar Polygons cylinder, pond body (14) lower end is tapered, and be divided into reaction chamber (2) and concentration compartments (6) are two-layer, mixing tank is loaded in the middle of the reaction chamber (2) or to be located at the pond separately external, connect water inlet pipe (18), stabilier (12) is installed in concentration compartments (6), shore pipe (10) is installed in the cone lower end, between concentration compartments (6) and the distributing water room (3) the pressure rising pipe (9) that is connected is housed.
2, according to the efficient precipitation concentrating unit of claim 1, it is characterized in that the slot opening B=230-300mm of V-type frid, the high C=60-100mm of groove, flute length A=300-500mm, the floor plan spacing of two-layer V-type frid is 60-100mm.
3, according to the efficient precipitation concentrating unit of claim 1, it is characterized in that forcing the diameter of mud guiding tube (5) is 25-32mm, have into mud hole (13) on it, be provided with apart from V-type frid notch 50-100mm place and force mud guiding tube (5) the V-type frid that multilayer is parallel to be connected into one.
4,, it is characterized in that each parts can make with metal, rigid plastics or glass-reinforced plastic material according to the efficient precipitation concentrating unit of claim 1.
CN 88213116 1988-09-14 1988-09-14 Integral high-efficient precipitation and concentration device Withdrawn CN2035651U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 88213116 CN2035651U (en) 1988-09-14 1988-09-14 Integral high-efficient precipitation and concentration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 88213116 CN2035651U (en) 1988-09-14 1988-09-14 Integral high-efficient precipitation and concentration device

Publications (1)

Publication Number Publication Date
CN2035651U true CN2035651U (en) 1989-04-12

Family

ID=4846294

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 88213116 Withdrawn CN2035651U (en) 1988-09-14 1988-09-14 Integral high-efficient precipitation and concentration device

Country Status (1)

Country Link
CN (1) CN2035651U (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100503491C (en) * 2001-06-21 2009-06-24 库恩生态产品有限公司 Device for thickening or dewatering sludge, watery, sediments or the like, espeically surplus sludge in sewage treantment plants
CN100528281C (en) * 2005-04-18 2009-08-19 同济大学 Tilted-plated settlement pool
CN100540106C (en) * 2007-03-26 2009-09-16 张建臣 Dreg-liquid separator
CN101165465B (en) * 2006-10-16 2010-08-18 刘希平 Double tube stratified water collection device
CN102557326A (en) * 2010-12-08 2012-07-11 李进民 Solid-liquid separation apparatus and its application in sewage treatment device
CN103007590A (en) * 2012-12-31 2013-04-03 江西稀有稀土金属钨业集团有限公司 Sedimentation device
CN104624393A (en) * 2013-11-08 2015-05-20 中冶长天国际工程有限责任公司 Multi-layer de-sliming thickener
CN105498352A (en) * 2015-11-28 2016-04-20 綦江县狮子桥供水有限公司 Waterworks sedimentation device

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100503491C (en) * 2001-06-21 2009-06-24 库恩生态产品有限公司 Device for thickening or dewatering sludge, watery, sediments or the like, espeically surplus sludge in sewage treantment plants
CN100528281C (en) * 2005-04-18 2009-08-19 同济大学 Tilted-plated settlement pool
CN101165465B (en) * 2006-10-16 2010-08-18 刘希平 Double tube stratified water collection device
CN100540106C (en) * 2007-03-26 2009-09-16 张建臣 Dreg-liquid separator
CN102557326A (en) * 2010-12-08 2012-07-11 李进民 Solid-liquid separation apparatus and its application in sewage treatment device
CN103007590A (en) * 2012-12-31 2013-04-03 江西稀有稀土金属钨业集团有限公司 Sedimentation device
CN104624393A (en) * 2013-11-08 2015-05-20 中冶长天国际工程有限责任公司 Multi-layer de-sliming thickener
CN105498352A (en) * 2015-11-28 2016-04-20 綦江县狮子桥供水有限公司 Waterworks sedimentation device

Similar Documents

Publication Publication Date Title
CN101569808B (en) Uninterrupted anti-disturbance flocculent deposit reverse separation system
CN2035651U (en) Integral high-efficient precipitation and concentration device
CN1876241A (en) Highly effective concentration technology for milltailings
CN107892437A (en) A kind of MBBR reaction systems of strengthened denitrification function
CN211056777U (en) Throw vertical high-efficient integration sewage treatment device of heavy medium
CN110526395A (en) Eddy flow anaerobic reactor for waste water treatment system
CN114573177A (en) Concentrated sewage treatment system of high-efficient sediment of double flute formula
FI57578C (en) ANALYSIS OF BIOLOGICAL TRAINING AV AVAILABLE
CN1513773A (en) High effect composite clarifying reaction pond and coagulating, precipitcting water treatment process
CN103408134B (en) Anaerobic sludge bed reactor and method for treating organic waste water by using same
CN207726766U (en) Flotation tank for water-oil separating
CN2848837Y (en) Soft magnetic ferrite grinding waste water treatment device
CN111233201B (en) Working face mine water solid removal device and solid removal process
CN107720956A (en) A kind of efficient double-cycling anaerobic reactor
CN201064679Y (en) Pipe chute coagulating sedimentation pool
CN203486964U (en) Anaerobic sludge red reactor
CN100337938C (en) Bioreactor for water treatment
CN207713487U (en) A kind of aerobic sludge reflux
CN2589465Y (en) Solid-liquid separating equipment
CN2491445Y (en) Efficiency anoxybiontic sewage treatment unit
CN218665705U (en) Integrated crude oil recovery and sump oil sludge reduction device
CN206408050U (en) Printing and dyeing wastewater treatment system
CN114906928B (en) Anaerobic reactor
CN216764452U (en) IC anaerobic reactor suitable for citric acid waste water treatment
CN217578658U (en) Improve storage mud pond and sludge treatment system of mud sedimentation efficiency

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C14 Grant of patent or utility model
GR01 Patent grant
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