CN110180228A - A kind of anti-gravity formula precipitation separation device for water treatment procedure - Google Patents
A kind of anti-gravity formula precipitation separation device for water treatment procedure Download PDFInfo
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- CN110180228A CN110180228A CN201910578262.9A CN201910578262A CN110180228A CN 110180228 A CN110180228 A CN 110180228A CN 201910578262 A CN201910578262 A CN 201910578262A CN 110180228 A CN110180228 A CN 110180228A
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- water
- tower
- gravity
- treatment procedure
- separation device
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/02—Settling tanks with single outlets for the separated liquid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/26—Separation of sediment aided by centrifugal force or centripetal force
Abstract
The present invention relates to a kind of anti-gravity formula precipitation separation devices for water treatment procedure, including high tower (13), water storage is equipped at the top of high tower (13) with head tank (4), intermediate in tower is gravity Disengagement zone (5), bottom precipitation area (6), the head tank (4) passes through high-order water-supply-pipe (10) and connects high tower (13) lower water inlet (1), high pressure water enters Ta Nei Gravity Separation area (5) from water inlet (1), and the rotary water current of spiral adverse current uplink is formed along high inner wall of tower, it is contacted with the object to be processed inputted from top of tower, liquid mixture is discharged from top delivery port (3), sediment lowers into settling zone (6) under the effect of gravity.Compared with prior art, the present invention makes simple, low in cost, portable and effective, good separating effect, and low energy consumption, and occupied area is small, and anti-gravity filter device is added separation force, realizes the continuity and completeness of separation, collectively promotes separation of solid and liquid.
Description
Technical field
The present invention relates to a kind of separators, and in particular to a kind of anti-gravity formula precipitation and separation dress for water treatment procedure
It sets.
Background technique
Separation of solid and liquid is one of most common operation in the industries such as chemistry, chemical industry, pharmacy, metallurgy, environmental protection, is non-equal
The mutually important component of separation, in many experimental implementations and production unit, separator is to influence experiment effect and product
The important link of quality.Current separation of solid and liquid process is divided into sedimentation separation and is separated by filtration, and wherein sedimentation separation is according to promotion
Power can be divided into gravitational settling, centrifugal force sedimentation and electromagnetic force sedimentation；Be separated by filtration according to motive force can be divided into gravity filtration,
Vacuum filter, pressure filtration and centrifugal force filtering etc..Pollution in order to avoid filter cloth, filter paper or filter membrane to filtrate, generallys use
Gravitational settling or centrifugal force sedimentation.However, centrifugal force sedimentation needs to introduce external motive force, can not expire under the conditions of part Experiment
Foot, therefore gravitational settling is often used as most simple and easy Precipitation Separation Technique.Therefore as can completing gravity in a container
Settle with separate two processes will bringing great convenience property for lock out operation.
Need to use separation of solid and liquid during Industrial Waste Water Treatments, Industrial Waste Water Treatments are to guarantee environment, ecology and health
Main means.For the ingredient in industrial wastewater, is separated and recovered while processing, resource is enabled to obtain sufficiently
It utilizes.However, traditional Industrial Waste Water Treatments, are not precipitated or precipitation and separation effect are poor, cause the effect of sewage treatment
Rate is low, the requirement for making it be difficult to meet current industrial sewage treatment.In addition, there are energy consumptions for traditional Industrial Waste Water Treatments process
Greatly, many drawbacks such as pollution is more, takes time and effort.
Chinese patent CN207838381U discloses a kind of trade effluent precipitation separation device, including stirring precipitation cylinder, institute
The upper end middle position for stating stirring precipitation cylinder has been arranged vertically upwards stirring transmission shaft by bearing holder (housing, cover), stirs the upper end of transmission shaft
Level is coaxially installed with transmission gear, stirs the stirring precipitation cylinder upper end on the right side of transmission shaft and partly inlays setting by motor installing frame
There is stirring motor, the upper end of stirring motor cooperates rotate gear by machine shaft, and the lower end for stirring transmission shaft protrudes into stirring and sinks
In the cylinder of shallow lake and it is provided with paddle group, the middle position on the left of precipitation cylinder is stirred and is provided with inlet tube, stir the right side of precipitation cylinder
Upper end is provided with overflow outlet pipe horizontally to the right, and the left end of overflow outlet pipe, which is inlayed, is provided with suction pump.The device is more
Using electrical equipment, the device rate of exchange are complicated, are not convenient to use.
Chinese patent CN205241308U discloses a kind of precipitation separation device, which includes precipitating groove body；The groove body
Lower part is the tubular groove body of taper, is equipped with overflow weir on the upper edge around groove body, is equipped with drain pipe at overflow weir weir bottom；In groove body
It bores bottom and is equipped with outer sludge pipe；It is interior that this is interior to be located at every cylinder vertical center in precipitating groove body middle and lower part every cylinder, in every cylinder bottom with
The taper cylindrical inner wall of groove body is affixed, is equipped with mud hole every cylinder lower part inside；Upper sedimentation Turbogrid plates；The sedimentation Turbogrid plates are to be fixed on
Precipitating in groove body upper inside wall, section is grid shape, vertical pipe group；Lower sedimentation Turbogrid plates；The sedimentation Turbogrid plates are to fix
Inside every in cylinder upper inside wall, section be grid shape, vertical pipe group；Feed pipe, the feed pipe are by under precipitating groove body
Portion's taper barrel tangentially enters groove body along groove body inner wall.
From the point of view of practical application effect, precipitation separation device disclosed in patent CN205241308U there are it is following not
Foot: (1) due to using natural sedimentation, cause the sedimentation time long.(2) after precipitating object amount increase, the passability of waste water declines, and causes
Treatment effect decline.(3) structure is more complex, and channel path is tortuous, leads to the easy fouling of pipeline, separating effect is made to be deteriorated.(4) it does not set
The problems such as meter precipitates outlet, few there are sediment derived quantity, causes the problems such as precipitation and separation exports low efficiency.
Summary of the invention
It is an object of the present invention to overcome the above-mentioned drawbacks of the prior art and provide one kind for water-treated
The anti-gravity formula precipitation separation device of journey.
The purpose of the present invention can be achieved through the following technical solutions: a kind of anti-gravity formula for water treatment procedure is heavy
Shallow lake separator, which is characterized in that including high tower, water storage head tank is equipped at the top of high tower, centre is gravity Disengagement zone in tower,
Bottom precipitation area, the head tank pass through high-order water-supply-pipe and connect high tower lower water inlet, and high pressure water enters from the inlet tower
Interior Gravity Separation area, and along the rotary water current of high inner wall of tower formation spiral adverse current uplink, with the object to be processed inputted from top of tower
Contact, liquid mixture are discharged from top delivery port, and sediment lowers into settling zone under the effect of gravity.
The pairs of diagonal position of water outlet and water inlet is arranged, and wherein water outlet is located at Gravity Separation area top tower body
On, water inlet is located in Gravity Separation area bottom tower body.The high-order water-supply-pipe is equipped with adjusting control valve, can automatically adjust
Water flow.
The high inner wall of tower is cylindrical, and high pressure water enters in high tower along a tangential direction, and forms the circle of bottom in and top out
Cartridge type water flow structure.Decline precipitating using the effect of gravity in retrograde water flow.Regular water flowing is conducive to precipitating
Sedimentation, reaches preferable separating effect.Water flow is adjusted using water head tank come regime flow and by automatic regulating valve, it is real
The continuity and completeness now separated improves separative efficiency.
The settling zone is equipped with resistance rotating plate, which forms grid configuration by vertical partition plate.
Sediment settles from top to bottom in the object to be processed, and the lattice-shaped by the way that high tower lower part is arranged in hinders rotating plate,
Into the settling zone of lower section.
The settling zone bottom is equipped with precipitating discharge outlet.
The precipitating discharge outlet connects discharge tube, and discharge tube is equipped with vent valves.
The device further includes water pump, the water pump head tank described by penstocks connection, using head tank come
Regime flow.
Present apparatus concrete operating principle is,
The specific stroke of water flow are as follows: high-order trough inner water is injected into high tower lower part through penstocks by water flow adjusting control valve,
Spiral adverse current uplink water flow is formed along high inner wall of tower, water outlet of the water flow on high tower top is discharged；
Precipitate specific stroke are as follows: due to gravity, precipitating settles from top to bottom in high tower, and precipitating is by being arranged in high tower
The lattice-shaped of lower part hinders rotating plate, and into the precipitating stagnant zone below Turbogrid plates, precipitating is collected into high tower bottom, periodically through heavy
The discharge of shallow lake discharge outlet.
Compared with prior art, the invention has the following advantages:
1, good separating effect, regular water flowing are conducive to the sedimentation of precipitating；
2, low energy consumption, using water head tank come regime flow, and is adjusted by automatic regulating valve；
3, occupied area is small, and separative efficiency is high, and energy conservation and environmental protection is time saving and energy saving；
4, anti-gravity filter device is added separation force, realizes the continuity and completeness of separation, collectively promotes solid
Liquid separation.
5, separation demand lasting, long-term, that amount is big can be met, without adding chemical agent, easy to maintain, inexpensive physics
Separator provides the water process anti-gravity formula precipitation separation device that one kind is economical and practical, efficient, safe, can be used for a long time.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of one embodiment of the invention device；
Fig. 2 is water outlet schematic cross-section in high tower tower body；
Fig. 3 is schematic cross-section at high tower tower body internal resistance rotating plate；
In figure: 1- water inlet, 2- resistance rotating plate, 3- water outlet, 4- head tank, 5- Gravity Separation area, the settling zone 6-, 7- precipitating
Discharge outlet, 8- vent valves, 9- adjusting control valve, 10- high position water-supply-pipe, 11- penstocks, 12- water pump, 13- high tower.
Specific embodiment
The present invention is described in detail with specific embodiment below in conjunction with the accompanying drawings.
Embodiment
As shown in Figures 1 to 3, a kind of anti-gravity formula precipitation separation device for water treatment procedure, structural schematic diagram is such as
Shown in Fig. 1, comprising: a high tower 13, inside are equipped with the accommodating space of water flow and precipitating；One water inlet 1 is set to 13 lower part of high tower,
Water inlet 1 is equipped with adjusting control valve 9, and hydraulic pressure is entered 13 lower part of high tower by high-order water-supply-pipe 10；One water outlet 3 is set to height
On tower 13 with the catercorner position of water inlet 1；One head tank 4 is set to 13 top of high tower, is connected with high-order water-supply-pipe 10；
One Gravity Separation area 5 is located at 13 middle part of high tower；One resistance rotating plate 2, is set to 13 lower part of high tower；One settling zone 6 is set to 13 bottom of high tower
Portion, 6 bottommost of settling zone are equipped with precipitating discharge outlet 7.
13 tower body of high tower is tubular structure, and top does not have top cover, and tower body is canister, water inlet 1 and all edges of water outlet 3
Round tangential direction is separately positioned on the lower part of tower body and the position of Upper diagonal line, forms the rotation water slowly moved upwards
Stream.The resistance rotating plate 2 of lattice-shaped is equipped with above the bottom of tower, since gravity declines precipitating, precipitating is entered by resistance rotating plate 2
The precipitating stagnant zone 6 of lower section passes through the heavy of tower bottom once the precipitating stagnant zone 6 that precipitating is fallen into below grid will be collected
Shallow lake discharge outlet 7 is discharged.Water pump 12 connects the head tank 4 by penstocks 11, using head tank come regime flow
When present apparatus specific works, the specific stroke of water flow are as follows: water is by water flow adjusting control valve 9 through a high position in head tank 4
Water-supply-pipe 10 is injected into 13 lower part of high tower, forms spiral adverse current uplink water flow, water outlet of the water flow on high tower top along high inner wall of tower
Mouth 3 is discharged, and object to be processed inside investment tower body, precipitates specific stroke at the top of high tower are as follows: due to gravity, precipitates in high tower
It settles, is sufficiently acted on the water flow of adverse current uplink from top to bottom, liquid is discharged after mixing with water from water outlet 3, and precipitating is by setting
It sets the lattice-shaped in high tower lower part and hinders rotating plate 2, into the precipitating stagnant zone 6 below Turbogrid plates, precipitating is collected into high tower bottom
Portion is periodically discharged through precipitating discharge outlet 7.
When using the present apparatus, following steps can be used:
(1) adjusting control valve 9 is opened, water inlet 1 is communicated by high-order water-supply-pipe 10 with high tower, water is formed in high tower
Spiral is driven in the wrong direction ascending current, and is discharged in the water outlet 3 of the diagonal positions of high tower top water inlet 1；
(2) since gravity declines precipitating, rotating plate 2 is hindered by the way that the lattice-shaped below tower is arranged in, into Turbogrid plates
The precipitating stagnant zone 6 of lower section；
(3) precipitating discharge outlet 7 is opened, the precipitating being collected is discharged by precipitating discharge outlet 7.
The above description of the embodiments is intended to facilitate ordinary skill in the art to understand and use the invention.
Person skilled in the art obviously easily can make various modifications to these embodiments, and described herein general
Principle is applied in other embodiments without having to go through creative labor.Therefore, the present invention is not limited to the above embodiments, ability
Field technique personnel announcement according to the present invention, improvement and modification made without departing from the scope of the present invention all should be of the invention
Within protection scope.
Claims (9)
1. a kind of anti-gravity formula precipitation separation device for water treatment procedure, which is characterized in that including high tower (13), high tower
(13) top is equipped with water storage with head tank (4), and intermediate in tower is gravity Disengagement zone (5), bottom precipitation area (6), the high position
Slot (4) passes through high-order water-supply-pipe (10) and connects high tower (13) lower water inlet (1), and high pressure water enters weight in tower from water inlet (1)
Power Disengagement zone (5), and along the rotary water current of high inner wall of tower formation spiral adverse current uplink, it is connect with the object to be processed inputted from top of tower
Touching, liquid mixture are discharged from top delivery port (3), and sediment lowers into settling zone (6) under the effect of gravity.
2. a kind of anti-gravity formula precipitation separation device for water treatment procedure according to claim 1, which is characterized in that
Diagonal position is arranged the water outlet (3) and water inlet (1) in pairs, and wherein water outlet (3) is located at Gravity Separation area (5) top
On tower body, water inlet (1) is located in Gravity Separation area (5) bottom tower body.
3. a kind of anti-gravity formula precipitation separation device for water treatment procedure according to claim 1, which is characterized in that
Described high tower (13) inner wall is cylindrical, and high pressure water enters in high tower along a tangential direction, and forms the drum type brake of bottom in and top out
Water flow structure.
4. a kind of anti-gravity formula precipitation separation device for water treatment procedure according to claim 1, which is characterized in that
The settling zone (6) is equipped with resistance rotating plate (2), which forms grid configuration by vertical partition plate.
5. a kind of anti-gravity formula precipitation separation device for water treatment procedure according to claim 4, which is characterized in that
Sediment settles from top to bottom in the object to be processed, and the lattice-shaped by the way that high tower lower part is arranged in hinders rotating plate (2), under
The settling zone (6) of side.
6. a kind of anti-gravity formula precipitation separation device for water treatment procedure according to claim 1, which is characterized in that
Settling zone (6) bottom is equipped with precipitating discharge outlet (7).
7. a kind of anti-gravity formula precipitation separation device for water treatment procedure according to claim 1, which is characterized in that
The precipitating discharge outlet (7) connects discharge tube, and discharge tube is equipped with vent valves (8).
8. a kind of anti-gravity formula precipitation separation device for water treatment procedure according to claim 1, which is characterized in that
The device further includes water pump (12), the water pump head tank (4) described by penstocks (11) connection.
9. a kind of anti-gravity formula precipitation separation device for water treatment procedure according to claim 1, which is characterized in that
The high-order water-supply-pipe (10) is equipped with adjusting control valve (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910578262.9A CN110180228A (en) | 2019-06-28 | 2019-06-28 | A kind of anti-gravity formula precipitation separation device for water treatment procedure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910578262.9A CN110180228A (en) | 2019-06-28 | 2019-06-28 | A kind of anti-gravity formula precipitation separation device for water treatment procedure |
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| Publication Number | Publication Date |
|---|---|
| CN110180228A true CN110180228A (en) | 2019-08-30 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910578262.9A Pending CN110180228A (en) | 2019-06-28 | 2019-06-28 | A kind of anti-gravity formula precipitation separation device for water treatment procedure |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3676208B2 (en) * | 2000-08-22 | 2005-07-27 | 株式会社西原環境テクノロジー | Solid-liquid separation tank |
| CN2782219Y (en) * | 2004-12-24 | 2006-05-24 | 化学工业部连云港设计研究院 | Hydraulic power separator |
| CN201197959Y (en) * | 2008-05-27 | 2009-02-25 | 李炳群 | Mud ore separator |
| CN101781032A (en) * | 2009-01-20 | 2010-07-21 | 扬州兄弟环境保护设备工程有限公司 | Coal slurry purifier |
| CN202570362U (en) * | 2008-12-22 | 2012-12-05 | 奥图泰有限公司 | A hindered-bed separator for separating particles in hydrous slurry |
-
2019
- 2019-06-28 CN CN201910578262.9A patent/CN110180228A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3676208B2 (en) * | 2000-08-22 | 2005-07-27 | 株式会社西原環境テクノロジー | Solid-liquid separation tank |
| CN2782219Y (en) * | 2004-12-24 | 2006-05-24 | 化学工业部连云港设计研究院 | Hydraulic power separator |
| CN201197959Y (en) * | 2008-05-27 | 2009-02-25 | 李炳群 | Mud ore separator |
| CN202570362U (en) * | 2008-12-22 | 2012-12-05 | 奥图泰有限公司 | A hindered-bed separator for separating particles in hydrous slurry |
| CN101781032A (en) * | 2009-01-20 | 2010-07-21 | 扬州兄弟环境保护设备工程有限公司 | Coal slurry purifier |
Non-Patent Citations (1)
| Title |
|---|
| 徐博: "《选煤知识问答》", 31 October 2013 * |
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Application publication date: 20190830 |