CN202569669U - Depositing tank for 1, 3-dimedone solid-liquid separation - Google Patents
Depositing tank for 1, 3-dimedone solid-liquid separation Download PDFInfo
- Publication number
- CN202569669U CN202569669U CN 201220113293 CN201220113293U CN202569669U CN 202569669 U CN202569669 U CN 202569669U CN 201220113293 CN201220113293 CN 201220113293 CN 201220113293 U CN201220113293 U CN 201220113293U CN 202569669 U CN202569669 U CN 202569669U
- Authority
- CN
- China
- Prior art keywords
- clear liquid
- tank body
- drainage tube
- solid
- tank
- 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.)
- Expired - Fee Related
Links
Images
Landscapes
- Cyclones (AREA)
Abstract
The utility model discloses a depositing tank for 1, 3-dimedone solid-liquid separation. The depositing tank comprises a bottom tapered tank body, a feed port, an exhaust port, a manhole, a discharge port and a clear liquid flow guide pipe are arranged on the tank body, the feed port and the exhaust port are symmetrically distributed at the top of the bottom tapered tank body, the manhole is arranged in the middle of the bottom tapered tank body, the discharge port is arranged at the bottom of the bottom tapered tank body, all pipe orifices are communicated with relative devices through a flange, a valve and a pipeline, the clear liquid flow guide pipe is arranged at the upper end of the boundary of clear liquid and deposit in the depositing tank taper, the mixing quantity of the clear liquid and the deposit is small (the deposit falling on the upper portion of the clear liquid flow guide pipe can be taken out under the condition that the clear liquid quickly flows out), secondary treating is omitted, material waste is reduced, and production efficiency is remarkably improved.
Description
Technical field
The utility model belongs to the container of Separation of Solid and Liquid, is specifically related to a kind ofly be used for 1, separates the settling tank of feed liquid and pressed powder in hydroresorcinol or other industrial products production process.
Background technology
In commercial production, often will utilize settling tank separating liquid and sediment, for example 1, be in order to separate feed liquid and metallic catalyst in the hydroresorcinol production, and sediment is because proportion is distributed in the tank base zone through post precipitation more greatly.General settling tank is bottom valve to be opened the back earlier sediment is emitted, and treats to change after sediment is put only again and discharges supernatant liquor.The defective that this method exists is: the conversion of sediment and supernatant liquor does not have obvious limit; The sediment that is positioned at blow-off valve doorway vertical direction receives gravity and flow action to take the lead in flowing out; Then the clear liquid on the upper strata sediment that just begins to drive the discharge gate periphery mixes outflow thereupon, and the conversion clear liquid is discharged again after the basic emptying of sediment.And be mixed with a considerable amount of clear liquids in the sediment of discharging, must the sediment of discharging be carried out after-treatment or ignore slatterning.
Summary of the invention
In order to address the above problem, the purpose of the utility model is, provides a kind of and is used for 1, and the settling tank of hydroresorcinol Separation of Solid and Liquid solves existing feed liquid settling tank part clear liquid and mixes with sediment, need carry out the problem of after-treatment or feed liquid waste.
The utility model provides a kind ofly is used for 1, the settling tank of hydroresorcinol Separation of Solid and Liquid, and it comprises base cone shape tank body; Tank body is provided with charging aperture, exhaust outlet, manhole, discharging opening, clear liquid drainage tube; Charging aperture and exhaust outlet are symmetrically distributed in base cone shape tank body top, and the centre is a manhole, and the tank body conical lower portion is a discharging opening; All mouths of pipe all are communicated with relevant apparatus through flange, valve, pipeline; This point is identical with all general settling tanks, and different is said settling tank cone clear liquid and upper end, sediment line of demarcation, is provided with a clear liquid drainage tube.Said clear liquid drainage tube extends inward into taper tank body center position through tank body, and the said clear liquid drainage tube mouth of pipe extends inward into taper tank body center position through tank body, and the clear liquid drainage tube mouth of pipe is inclined upwardly a little, in order to avoid retain feed liquid in the pipe.The acute angle angle of said clear liquid drainage tube mouth of pipe place for leaving downwards is in order to avoid sediment falls into.
The utility model provides a kind ofly is used for 1; The settling tank of hydroresorcinol Separation of Solid and Liquid, its beneficial effect are that clear liquid only has mixing of minute quantity with sediment; The sediment that falls within clear liquid drainage tube top flows out under the too fast situation and can be taken out of at clear liquid; Need not to carry out after-treatment, reduced the waste of material, production efficiency is significantly improved.
Description of drawings
Fig. 1 is the overall structure sketch map of an embodiment of the utility model.
Mark among the figure:
1. base cone shape tank body; 2. charging aperture; 3. discharging opening; 4. valve; 5. clear liquid drainage tube; 6. exhaust outlet; 7. clear liquid and sediment line of demarcation; 8. manhole.
The specific embodiment
With reference to the accompanying drawings, in conjunction with an embodiment, a kind ofly be used for 1 to what the utility model provided, the settling tank of hydroresorcinol or other products Separation of Solid and Liquid carries out detailed explanation.
Embodiment
With reference to Fig. 1; The a kind of of present embodiment is used for 1, the settling tank of hydroresorcinol Separation of Solid and Liquid, and it comprises base cone shape tank body 1, charging aperture 2, exhaust outlet 6, manhole 8, discharging opening 3, clear liquid drainage tube 5; Charging aperture 2 is symmetrically distributed in base cone shape tank body 1 top with exhaust outlet 6; The centre is a manhole 8, and the tank body conical lower portion is a discharging opening 3, and all mouths of pipe all are communicated with relevant apparatus through flange, valve, pipeline; Said settling tank cone clear liquid and 7 upper ends, sediment line of demarcation are provided with a clear liquid drainage tube 5.The mouth of pipe of said clear liquid drainage tube 5 extends inward into base cone shape tank body 1 center position through tank body, and the clear liquid drainage tube mouth of pipe is inclined upwardly a little.The mouth of pipe of said clear liquid drainage tube 5 is downward acute angle angle.
With 1, hydroresorcinol adds in the settling tanks through charging aperture 2, and after a period of time, clear liquid is demarcated with sediment, and at this moment, base cone shape tank body 1 bottom valve 4 state that keeps shut is opened clear liquid drainage tube 5, and clear liquid is carried out drainage.Clear liquid drainage tube 5 can carry out drainage to clear liquid fast, and drainage after finishing is opened base cone shape tank body 1 bottom valve 4, and sediment is emitted.The sediment that has minute quantity in the clear liquid need not to carry out subsequent processes, has reduced the waste of material, and production efficiency is significantly improved.
With 1, the hydroresorcinol feed liquid adds in the polyethylene settling tank, after several hours through charging aperture; Can be observed supernatant liquor and the catalyst precipitation deposits yields is obviously demarcated; At this moment, slowly open clear liquid drainage tube valve, avoid the minute quantity catalyst that is deposited in drainage tube top is taken out of as far as possible.The supernatant liquor that drains carries out secondary filter on demand, because remainder catalyst seldom is difficult for blocking filter cloth in the clear liquid, post processing work is comparatively smooth and easy.After the clear liquid drainage finished, with the tank base valve open, catalyst was emitted otherwise processed.If do not adopt the clear liquid drainage tube, must at first emit catalyst from bottom valve, this process can cause the part clear liquid to mix unclear with solid catalyst and need secondary separation, numerous and diverse, the decrease in efficiency of production process.
Claims (3)
1. one kind is used for 1, and the settling tank of hydroresorcinol Separation of Solid and Liquid is characterized in that: it comprises base cone shape tank body; Tank body is provided with charging aperture, exhaust outlet, manhole, discharging opening, clear liquid drainage tube, and charging aperture and exhaust outlet are symmetrically distributed in base cone shape tank body top, and the centre is a manhole; The tank body conical lower portion is a discharging opening; All mouths of pipe all are communicated with relevant apparatus through flange, valve, pipeline, and said settling tank cone clear liquid and upper end, sediment line of demarcation are provided with a clear liquid drainage tube.
2. according to claim 1ly be used for 1, the settling tank of hydroresorcinol Separation of Solid and Liquid is characterized in that: the said clear liquid drainage tube mouth of pipe extends inward into taper tank body center position through tank body, and the clear liquid drainage tube mouth of pipe is inclined upwardly a little.
3. according to claim 2ly be used for 1, the settling tank of hydroresorcinol Separation of Solid and Liquid is characterized in that: the acute angle angle of said clear liquid drainage tube mouth of pipe place for leaving downwards.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220113293 CN202569669U (en) | 2012-03-16 | 2012-03-16 | Depositing tank for 1, 3-dimedone solid-liquid separation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220113293 CN202569669U (en) | 2012-03-16 | 2012-03-16 | Depositing tank for 1, 3-dimedone solid-liquid separation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202569669U true CN202569669U (en) | 2012-12-05 |
Family
ID=47239126
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220113293 Expired - Fee Related CN202569669U (en) | 2012-03-16 | 2012-03-16 | Depositing tank for 1, 3-dimedone solid-liquid separation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202569669U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103467278A (en) * | 2013-09-25 | 2013-12-25 | 威海韩孚生化药业有限公司 | Preparation method and device of 2,4-dichlorphenoxyacetic acid |
| CN104630471A (en) * | 2015-03-01 | 2015-05-20 | 云南驰宏锌锗股份有限公司 | Method and device for removing magnesium ions in zinc sulfate solution by virtue of pressure |
| CN105013218A (en) * | 2015-08-05 | 2015-11-04 | 安吉捷达贸易有限公司 | Depositing tank used for accurate separation of 1, 3-cyclohexanedione solid and liquid |
| CN104998442B (en) * | 2015-08-05 | 2016-06-08 | 安吉捷达贸易有限公司 | The settling tank of hydroresorcinol solid-liquid clean cut separation |
-
2012
- 2012-03-16 CN CN 201220113293 patent/CN202569669U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103467278A (en) * | 2013-09-25 | 2013-12-25 | 威海韩孚生化药业有限公司 | Preparation method and device of 2,4-dichlorphenoxyacetic acid |
| CN103467278B (en) * | 2013-09-25 | 2015-04-08 | 威海韩孚生化药业有限公司 | Preparation method and device of 2,4-dichlorphenoxyacetic acid |
| CN104630471A (en) * | 2015-03-01 | 2015-05-20 | 云南驰宏锌锗股份有限公司 | Method and device for removing magnesium ions in zinc sulfate solution by virtue of pressure |
| CN105013218A (en) * | 2015-08-05 | 2015-11-04 | 安吉捷达贸易有限公司 | Depositing tank used for accurate separation of 1, 3-cyclohexanedione solid and liquid |
| CN104998442B (en) * | 2015-08-05 | 2016-06-08 | 安吉捷达贸易有限公司 | The settling tank of hydroresorcinol solid-liquid clean cut separation |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202569669U (en) | Depositing tank for 1, 3-dimedone solid-liquid separation | |
| CN203004077U (en) | Concrete sand-stone separation and slurry recovery environmental-protection apparatus | |
| CN102011001B (en) | Feeding device and method for cadmium-removing boiling purification tank system | |
| CN105036397A (en) | Waste water treatment system capable of achieving gradation and self-filtration of sludge | |
| CN206624871U (en) | Sand setting for anaerobic fermentation removes system | |
| CN203620394U (en) | Separating device for rear-earth particles in waste liquor | |
| CN203663502U (en) | Oil and water two-phase liquid separation system | |
| CN203139702U (en) | Washing, sedimentation and deslagging device of recycling sand | |
| CN103803627B (en) | Separation and impurity removal method of white mud/calcium carbide residue-gypsum process based desulfurization gypsum slurry | |
| CN202390434U (en) | Biogas generating device for discharging sand through automatic flow | |
| CN203474794U (en) | Spiral type biogas fermentation tank capable of automatically discharging residues | |
| CN204523259U (en) | Flotation calcium oxide constant voltage chemicals dosing plant | |
| CN202155078U (en) | Material setting tank | |
| CN107297091A (en) | A kind of settler for possessing automatic mud removing function | |
| CN203319763U (en) | IC (internal circulation) anaerobic reactor | |
| CN207845358U (en) | A kind of full-automatic separation of solid and liquid sewage disposal system | |
| CN205892832U (en) | High -efficient high turbidity water purifier | |
| CN205392162U (en) | Magnesium oxide method desulfurizing tower with anti - washing unit | |
| CN205549837U (en) | Rotatory device that deposits | |
| CN205627207U (en) | Sewage treatment carries sand machine | |
| CN205518172U (en) | Concrete residue separator | |
| CN201971877U (en) | Feeding device for cadmium removal boiling purification trough system | |
| CN206867776U (en) | A kind of environment protection sewage settling tank | |
| CN218811281U (en) | A high-efficient sludge concentration device for cement plant | |
| CN202983301U (en) | Automatic micro-powder sorting equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Process for desalting 1,3-propylene glycol fermentation liquor by electricity dialysis Effective date of registration: 20140513 Granted publication date: 20121205 Pledgee: Qingdao high technology financing Company limited by guarantee Pledgor: Qingdao Yimingxiang Fine Chemical Co., Ltd. Registration number: 2014990000345 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20150811 Granted publication date: 20121205 Pledgee: Qingdao high technology financing Company limited by guarantee Pledgor: Qingdao Yimingxiang Fine Chemical Co., Ltd. Registration number: 2014990000345 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Process for desalting 1,3-propylene glycol fermentation liquor by electricity dialysis Effective date of registration: 20150826 Granted publication date: 20121205 Pledgee: Qingdao high technology financing Company limited by guarantee Pledgor: Qingdao Yimingxiang Fine Chemical Co., Ltd. Registration number: 2015990000691 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121205 Termination date: 20190316 |