CN206252891U - A kind of settling tank with forecooler - Google Patents
A kind of settling tank with forecooler Download PDFInfo
- Publication number
- CN206252891U CN206252891U CN201621278598.1U CN201621278598U CN206252891U CN 206252891 U CN206252891 U CN 206252891U CN 201621278598 U CN201621278598 U CN 201621278598U CN 206252891 U CN206252891 U CN 206252891U
- Authority
- CN
- China
- Prior art keywords
- tank
- settling tank
- forecooler
- tank body
- upper lid
- 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
- 238000001556 precipitation Methods 0.000 claims abstract description 21
- 239000007788 liquid Substances 0.000 claims abstract description 18
- 238000000967 suction filtration Methods 0.000 claims abstract description 15
- 230000005540 biological transmission Effects 0.000 claims abstract description 11
- 238000000576 coating method Methods 0.000 claims abstract description 10
- 239000011248 coating agent Substances 0.000 claims abstract description 7
- 230000006835 compression Effects 0.000 claims abstract description 7
- 238000007906 compression Methods 0.000 claims abstract description 7
- 238000009413 insulation Methods 0.000 claims description 13
- 210000005069 ears Anatomy 0.000 claims description 4
- 230000008014 freezing Effects 0.000 claims description 3
- 238000007710 freezing Methods 0.000 claims description 3
- 229920002635 polyurethane Polymers 0.000 claims description 3
- 239000004814 polyurethane Substances 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims description 3
- 238000000108 ultra-filtration Methods 0.000 claims 1
- 238000000926 separation method Methods 0.000 abstract description 12
- 239000003960 organic solvent Substances 0.000 abstract description 10
- 238000000605 extraction Methods 0.000 abstract description 7
- 239000010410 layer Substances 0.000 abstract description 5
- 239000004809 Teflon Substances 0.000 abstract description 4
- 229920006362 Teflon® Polymers 0.000 abstract description 4
- 239000003513 alkali Substances 0.000 abstract description 4
- 230000001458 anti-acid effect Effects 0.000 abstract description 4
- 239000011241 protective layer Substances 0.000 abstract description 4
- 238000006243 chemical reaction Methods 0.000 description 8
- 239000007787 solid Substances 0.000 description 8
- 239000000706 filtrate Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- 239000012065 filter cake Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 238000011049 filling Methods 0.000 description 3
- 239000013049 sediment Substances 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000012824 chemical production Methods 0.000 description 2
- 150000002270 gangliosides Chemical class 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 210000002569 neuron Anatomy 0.000 description 2
- 239000000741 silica gel Substances 0.000 description 2
- 229910002027 silica gel Inorganic materials 0.000 description 2
- 208000020431 spinal cord injury Diseases 0.000 description 2
- 206010000117 Abnormal behaviour Diseases 0.000 description 1
- 241000208340 Araliaceae Species 0.000 description 1
- 208000012219 Autonomic Nervous System disease Diseases 0.000 description 1
- 235000005035 Panax pseudoginseng ssp. pseudoginseng Nutrition 0.000 description 1
- 235000003140 Panax quinquefolius Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 210000004556 brain Anatomy 0.000 description 1
- 230000008344 brain blood flow Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 235000008434 ginseng Nutrition 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000007830 nerve conduction Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 210000003296 saliva Anatomy 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Abstract
The utility model discloses a kind of settling tank with forecooler, including tank body, the tank body includes the upper lid and settling tank that are connected by flange, the upper lid is provided with transmission device and charging aperture, the settling tank is double tubular tank body, and settling tank bottom is connected with taper precipitation bucket, the stirred tank being connected with transmission device is provided with settling tank, the forecooler connected with tank body is additionally provided with upper lid, the taper precipitation bucket bottom is connected with Suction filtration device.The utility model is provided with forecooler on upper lid and precooling and can preserve extractant, efficient heat exchange is realized by compression refigerating machine, so that the temperature for reducing organic solvent has reached the requirement of low-temperature extraction；Solid-liquid separation efficiency can be improved by being provided with active Suction filtration device in tank body lower part；The coefficient of friction that Teflon coating effectively reduces inwall is provided with by inner tank wall, the performance of the antiacid alkali resistant of anticorrosion of vertical tank body is increased also by layer protective layer is provided with.
Description
Technical field
The utility model is related to chemical production equipment field, specifically refers to a kind of settling tank with forecooler.
Background technology
Monostalotetrahexosylgangliside is one of most important gangliosides, is obtained by being extracted in pig brain, can
To accelerate the reparation of damaged nerve cell, promote the growth and regeneration of nerve cell, improve nerve conduction etc., to brain blood flow power
Learn parameter and positive because causing encephaledema to play the role of after damage.It is mainly used in the reparation of maincenter and disorder of peripheral autonomic nervous system
And treatment, it is considered to be one of current clinical treatment spinal cord injury (SCI) maximally effective medicine；The single saliva of zoopery display
Liquid acid tetrahexose gangliosides can also improve the behavior disorder caused by Parkinson's.
Settling tank is to prepare important instrument during hydrolysis kettle Monostalotetrahexosylgangliside, mixed for solid-liquid
The device of compound stirring reaction, described device is settling tank, is made by being improved on general reactor, is generally existed
It is stirred after filling raw material, and is staticly settled again after stirring certain hour, so as to reaches the purpose of separation of solid and liquid.But it is existing
Settling tank can not reach good solid-liquid separation effect, and when needing to maintain certain low temperature process to react, without one kind
Preferable settling tank carries out precooling treatment.
Utility model content
The purpose of this utility model is to provide one kind to be provided with forecooler consequently facilitating low-temperature extraction is former by import
Expect and be obtained in that the settling tank of preferable sedimentation effect.
The utility model is achieved through the following technical solutions：A kind of settling tank with forecooler, including tank body, the tank
Body includes the upper lid and settling tank that are connected by flange, and the upper lid is provided with transmission device and charging aperture, and the settling tank is
Double tubular tank body, settling tank bottom is connected with taper precipitation bucket, and the stirred tank being connected with transmission device is provided with settling tank, on
The forecooler for being additionally provided with and being connected with tank body is covered, the taper precipitation bucket bottom is connected with Suction filtration device.Being used in of the present apparatus
In work production technology, such as, it is necessary to raw material is stirred and organic solvent low-temperature extraction is added and solid in the thick purifying process of silica gel
The isolated target solution of liquid, so the present apparatus is provided with forecooler on upper lid, needed for can organic solvent be cooled in advance
Temperature, so as to directly be filled into tank interior in reaction, improves extraction efficiency.And after mixing certain hour, sink
Material in the tank of shallow lake staticly settles a period of time, then carries out pressure suction filtration by the Suction filtration device of taper precipitation bucket bottom, from
And the effect of separation of solid and liquid is reached, and resulting filtrate is stored in be stored up and be for further processing in tank, and precipitated filter cakes
Focus in the lump, so as to complete the purpose of reaction precipitation separation.
Further, the forecooler includes heat insulation tank and the compression refigerating machine for freezing is connected with heat insulation tank.It is described
Organic solvent store in heat insulation tank, and lowered the temperature all the time by compression refigerating machine and kept the temperature at predetermined temperature value
In the range of, the connectivity part of heat insulation tank and tank body is just opened in reaction so as to complete the filling of organic solvent.
Further, the Suction filtration device includes the screen pipe being connected with taper precipitation bucket, and the screen pipe bottom is provided with
Vavuum pump, the vavuum pump side is provided with liquid outlet, and screen pipe is connected by flange with taper precipitation bucket bottom, and in screen pipe
It is provided with milipore filter.And described Suction filtration device is to form negative pressure in screen pipe bottom by vavuum pump so that taper precipitation bucket bottom
The sediment in portion is inhaled into screen pipe, and liquid therein is discharged by milipore filter into vavuum pump, and remaining precipitated filter cakes
Can be taken out by opening the flange of screen pipe, so as to reach the purpose of high efficient solid and liquid separation, it is also possible to reclaim filtrate as far as possible,
Reduce the loss of filtrate.
Further, the transmission device includes the motor being connected with stirred tank and the support for fixing motor.
Further, it is provided with polyurethane insulation coating outside the tank body.
Further, the inner tank wall is provided with polytetrafluorethylecoatings coatings.Described inner tank wall is provided with Teflon
Coating effectively reduces the coefficient of friction of inwall, and the anticorrosion that vertical tank body is increased also by layer protective layer is provided with is antiacid
The performance of alkali resistant.
Further, the precipitation tank wall is provided with for supporting picking up the ears for tank body.
Further, it is provided with thermometer in the settling tank.
The utility model compared with prior art, with advantages below and beneficial effect：
（1）The utility model is provided with forecooler on upper lid and precooling and can preserve extractant, by compression refigerating machine reality
Now efficient heat exchange, so that the temperature for reducing organic solvent has reached the requirement of low-temperature extraction, then directly adds in reaction
Note, improves extraction efficiency；
（2）The utility model can improve solid-liquid separation efficiency by being provided with active Suction filtration device in tank body lower part, subtract
The loss and waste of the filtrate formed after few Solvent Extract methods raw material object, are also prevented from the sedimentation effect of solution natural sedimentation
The halfway problem of difference separation of solid and liquid occurs；
（3）The utility model in inner tank wall by being provided with the friction system that Teflon coating effectively reduces inwall
Number, the performance of the antiacid alkali resistant of anticorrosion of vertical tank body is increased also by layer protective layer is provided with.
Brief description of the drawings
The detailed description made to non-limiting example with reference to the following drawings by reading, other spies of the present utility model
Levy, objects and advantages will become apparent：
Fig. 1 is structural representation of the present utility model.
Wherein：1-tank body, 2-upper lid, 3-settling tank, 4-taper precipitation bucket, 5-stirred tank, 6-forecooler, 7-
Screen pipe, 8-vavuum pump, 9-motor, 10-support, 11-pick up the ears, 12-thermometer
Specific embodiment
Embodiment of the present utility model is described below in detail, the example of the embodiment is shown in the drawings, wherein ad initio
Same or similar element or element with same or like function are represented to same or similar label eventually.Below by ginseng
The embodiment for examining Description of Drawings is exemplary, is only used for explaining the utility model, and it is not intended that to of the present utility model
Limitation.
In description of the present utility model, it is to be understood that term " " center ", " longitudinal direction ", " transverse direction ", " on ", D score,
The orientation or position relationship of the instruction such as "front", "rear", "left", "right", " vertical ", " level ", " top ", " bottom ", " interior ", " outward " are
Based on orientation shown in the drawings or position relationship, it is for only for ease of description the utility model and simplifies description, rather than instruction
Or imply that the device or element of meaning with specific orientation, with specific azimuth configuration and operation, therefore must not be understood that
It is to limitation of the present utility model.
, it is necessary to explanation, unless otherwise clearly defined and limited, term " is pacified in description of the present utility model
Dress ", " connected ", " connection " should be interpreted broadly, for example, it may be fixedly connected, or be detachably connected, or integratedly
Connection；Can mechanically connect, or electrically connect；Can also be joined directly together, or indirect by intermediary
It is connected, can is two connections of element internal.For the ordinary skill in the art, can be with concrete condition understanding
State concrete meaning of the term in the utility model.
Embodiment 1：
A kind of settling tank 3 with forecooler 6 of the present embodiment, as shown in figure 1, including tank body 1, the tank body 1 includes
The upper lid 2 and settling tank 3 connected by flange, the upper lid 2 are provided with transmission device and charging aperture, and the settling tank 3 is double
Layer tubular tank body 1, the bottom of settling tank 3 is connected with taper precipitation bucket 4, settling tank 3 and is provided with the stirred tank being connected with transmission device
5, the forecooler 6 connected with tank body 1 is additionally provided with upper lid 2, the bottom of taper precipitation bucket 4 is connected with Suction filtration device.The present apparatus
It is used in chemical production technology, such as, it is necessary to raw material is stirred and organic solvent low temperature is added in the thick purifying process of silica gel
Extract and separation of solid and liquid obtains target solution, so the present apparatus is provided with forecooler 6 on upper lid 2, can in advance by organic solvent
Required temperature is cooled to, so as to be directly filled into inside tank body 1 in reaction, extraction efficiency is improved.And pass through and mix one
After fixing time, the material in settling tank 3 staticly settles a period of time, is then entered by the Suction filtration device of the bottom of taper precipitation bucket 4
Row forces suction filtration, and so as to reach the effect of separation of solid and liquid, and resulting filtrate is stored in be stored up and be for further processing in tank,
And precipitated filter cakes are also focused in the lump, so as to complete the purpose of reaction precipitation separation.
Embodiment 2：
The present embodiment is on the basis of above-described embodiment, further to limit, the forecooler 6 include heat insulation tank and with
Heat insulation tank connection is used for the compression refigerating machine for freezing.Described organic solvent is stored in heat insulation tank, and is made all the time by compression
Cold is lowered the temperature and is kept the temperature in the range of predetermined temperature value, and the connection of heat insulation tank and tank body 1 is just opened in reaction
Place is so as to complete the filling of organic solvent.The other parts of the present embodiment are same as the previously described embodiments, repeat no more.
Embodiment 3：
The present embodiment is on the basis of above-described embodiment, further to limit, and it is heavy with taper that the Suction filtration device includes
The screen pipe 7 that the bucket 4 that forms sediment is connected, the bottom of the screen pipe 7 is provided with vavuum pump 8, and the side of the vavuum pump 8 is provided with liquid outlet, filtering
Pipe 7 is connected by flange with the bottom of taper precipitation bucket 4, and is provided with milipore filter in screen pipe 7.And described Suction filtration device is to pass through
Vavuum pump 8 forms negative pressure in the bottom of screen pipe 7 so that the sediment of the bottom of taper precipitation bucket 4 is inhaled into screen pipe 7, wherein
Liquid discharged into vavuum pump 8 by milipore filter, and remaining precipitated filter cakes can be taken by opening the flange of screen pipe 7
Go out, so as to reach the purpose of high efficient solid and liquid separation, it is also possible to reclaim filtrate as far as possible, reduce the loss of filtrate.The present embodiment
Other parts are same as the previously described embodiments, repeat no more.
Embodiment 4：
The present embodiment is on the basis of above-described embodiment, further to limit, and the transmission device includes and stirred tank 5
The motor 9 of connection and for fixing the support 10 of motor 9, and polyurethane insulation coating is provided with outside tank body 1, set on the inwall of tank body 1
There are polytetrafluorethylecoatings coatings.The described inwall of tank body 1 is provided with the coefficient of friction that Teflon coating effectively reduces inwall,
Increase the performance of the antiacid alkali resistant of anticorrosion of vertical tank body 1 by being provided with layer protective layer.Further, the settling tank 3
It is additionally provided with outer wall and pick up the ears 11 for support tank body 1, thermometer 12 is provided with settling tank 3.The other parts of the present embodiment with
Above-described embodiment is identical, repeats no more.
While there has been shown and described that embodiment of the present utility model, it will be understood by those skilled in the art that：
In the case where principle of the present utility model and objective is not departed from various changes, modification, replacement and modification can be carried out to these embodiments,
Scope of the present utility model is limited by claim and its equivalent.
Claims (8)
1. a kind of settling tank with forecooler, it is characterised in that：Including tank body（1）, the tank body（1）Including being connected by flange
The upper lid for connecing（2）And settling tank（3）, the upper lid（2）It is provided with transmission device and charging aperture, the settling tank（3）It is bilayer
Tubular tank body, settling tank（3）Bottom is connected with taper precipitation bucket（4）, settling tank（3）Inside it is provided with the stirring being connected with transmission device
Kettle（5）, upper lid（2）On be additionally provided with and tank body（1）The forecooler of connection（6）, the taper precipitation bucket（4）Bottom is connected with suction filtration
Device.
2. a kind of settling tank with forecooler according to claim 1, it is characterised in that：The forecooler（6）Including
Heat insulation tank and the compression refigerating machine for freezing is connected with heat insulation tank.
3. a kind of settling tank with forecooler according to claim 1 and 2, it is characterised in that：The Suction filtration device bag
Include and taper precipitation bucket（4）The screen pipe of connection（7）, the screen pipe（7）Bottom is provided with vavuum pump（8）, the vavuum pump（8）
Side is provided with liquid outlet, screen pipe（7）By flange and taper precipitation bucket（4）Bottom connects, and screen pipe（7）Inside it is provided with ultrafiltration
Film.
4. a kind of settling tank with forecooler according to claim 1 and 2, it is characterised in that：The transmission device bag
Include and stirred tank（5）The motor of connection（9）With for fixing motor（9）Support（10）.
5. a kind of settling tank with forecooler according to claim 1 and 2, it is characterised in that：The tank body（1）It is outside
It is provided with polyurethane insulation coating.
6. a kind of settling tank with forecooler according to claim 1 and 2, it is characterised in that：The tank body（1）Inwall
It is provided with polytetrafluorethylecoatings coatings.
7. a kind of settling tank with forecooler according to claim 1 and 2, it is characterised in that：The settling tank（3）Outward
Wall is provided with for supporting tank body（1）Pick up the ears（11）.
8. a kind of settling tank with forecooler according to claim 1 and 2, it is characterised in that：The settling tank（3）It is interior
It is provided with thermometer（12）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621278598.1U CN206252891U (en) | 2016-11-27 | 2016-11-27 | A kind of settling tank with forecooler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621278598.1U CN206252891U (en) | 2016-11-27 | 2016-11-27 | A kind of settling tank with forecooler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206252891U true CN206252891U (en) | 2017-06-16 |
Family
ID=59027870
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621278598.1U Expired - Fee Related CN206252891U (en) | 2016-11-27 | 2016-11-27 | A kind of settling tank with forecooler |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206252891U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110743476A (en) * | 2018-07-24 | 2020-02-04 | 唐山市丰南区奉岗灰业有限公司 | Multifunctional calcium hydroxide preparation tank and preparation method |
| CN113493873A (en) * | 2021-08-05 | 2021-10-12 | 深圳众意远诚环保科技有限公司 | Copper lithium extraction residual liquid recovery unit |
-
2016
- 2016-11-27 CN CN201621278598.1U patent/CN206252891U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110743476A (en) * | 2018-07-24 | 2020-02-04 | 唐山市丰南区奉岗灰业有限公司 | Multifunctional calcium hydroxide preparation tank and preparation method |
| CN110743476B (en) * | 2018-07-24 | 2021-07-06 | 唐山市丰南区奉岗灰业有限公司 | Multifunctional calcium hydroxide preparation tank and preparation method |
| CN113493873A (en) * | 2021-08-05 | 2021-10-12 | 深圳众意远诚环保科技有限公司 | Copper lithium extraction residual liquid recovery unit |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Gunbarrel with precooler Effective date of registration: 20180828 Granted publication date: 20170616 Pledgee: Luzhou Xinglu finance Company limited by guarantee Pledgor: LUZHOU RUIXING BIOENGINEERING CO.,LTD. Registration number: 2018510000087 |
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| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20190819 Granted publication date: 20170616 Pledgee: Luzhou Xinglu finance Company limited by guarantee Pledgor: LUZHOU RUIXING BIOENGINEERING CO.,LTD. Registration number: 2018510000087 |
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| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Gunbarrel with precooler Effective date of registration: 20190827 Granted publication date: 20170616 Pledgee: Luzhou Xinglu Financing Guarantee Group Co.,Ltd. Pledgor: LUZHOU RUIXING BIOENGINEERING CO.,LTD. Registration number: Y2019510000013 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Gunbarrel with precooler Effective date of registration: 20190827 Granted publication date: 20170616 Pledgee: Luzhou Xinglu Financing Guarantee Group Co.,Ltd. Pledgor: LUZHOU RUIXING BIOENGINEERING CO.,LTD. Registration number: Y2019510000013 |
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| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20200903 Granted publication date: 20170616 Pledgee: Luzhou Xinglu Financing Guarantee Group Co.,Ltd. Pledgor: LUZHOU RUIXING BIOENGINEERING Co.,Ltd. Registration number: Y2019510000013 |
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| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210413 Address after: 646100 Lingang Economic Park, Luxian Economic Development Zone, Luzhou City, Sichuan Province Patentee after: SICHUAN QIGEMAN PHARMACEUTICAL Co.,Ltd. Address before: 646116 Baihe Town, Luxian County, Luzhou City, Sichuan Province Patentee before: LUZHOU RUIXING BIOENGINEERING Co.,Ltd. |
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