CN205549639U - Bile acid enrichment facility - Google Patents
Bile acid enrichment facility Download PDFInfo
- Publication number
- CN205549639U CN205549639U CN201620269403.0U CN201620269403U CN205549639U CN 205549639 U CN205549639 U CN 205549639U CN 201620269403 U CN201620269403 U CN 201620269403U CN 205549639 U CN205549639 U CN 205549639U
- Authority
- CN
- China
- Prior art keywords
- concentration tank
- condenser
- chuck
- tank
- pipeline
- 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.)
- Active
Links
- HSINOMROUCMIEA-FGVHQWLLSA-N (2s,4r)-4-[(3r,5s,6r,7r,8s,9s,10s,13r,14s,17r)-6-ethyl-3,7-dihydroxy-10,13-dimethyl-2,3,4,5,6,7,8,9,11,12,14,15,16,17-tetradecahydro-1h-cyclopenta[a]phenanthren-17-yl]-2-methylpentanoic acid Chemical compound C([C@@]12C)C[C@@H](O)C[C@H]1[C@@H](CC)[C@@H](O)[C@@H]1[C@@H]2CC[C@]2(C)[C@@H]([C@H](C)C[C@H](C)C(O)=O)CC[C@H]21 HSINOMROUCMIEA-FGVHQWLLSA-N 0.000 title claims abstract description 15
- 239000003613 bile acid Substances 0.000 title claims abstract description 15
- 238000003756 stirring Methods 0.000 claims abstract description 17
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 230000007246 mechanism Effects 0.000 claims abstract description 9
- 239000012530 fluid Substances 0.000 claims abstract description 7
- 230000008676 import Effects 0.000 claims abstract description 3
- 238000007599 discharging Methods 0.000 claims description 8
- 239000006199 nebulizer Substances 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 238000000034 method Methods 0.000 abstract description 5
- 230000008569 process Effects 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract 1
- 238000007127 saponification reaction Methods 0.000 description 5
- 238000009835 boiling Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 238000001944 continuous distillation Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000012265 solid product Substances 0.000 description 2
- 238000005292 vacuum distillation Methods 0.000 description 2
- 241000287828 Gallus gallus Species 0.000 description 1
- 238000009360 aquaculture Methods 0.000 description 1
- 244000144974 aquaculture Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a bile acid enrichment facility. This bile acid enrichment facility, including concentrated jar, condenser and liquid -collecting tank, it presss from both sides the cover to be equipped with one at concentrated jar outside cover, a concentrated jar steam outlet who locates concentrated tank deck portion one side tells two the tunnel through the pipeline behind a vacuum pump, be linked together with the import of clamp cover medium all the way, another way is linked together with the feed inlet of condenser, it also is linked together with the feed inlet of condenser through the pipeline to press from both sides the export of cover medium, the discharge gate of condenser is linked together through the feed inlet of a condensate delivery pump with liquid -collecting tank through the pipeline. This bile acid enrichment facility, it is mobile at concentrated jar inner loop through the stirring messenger extract of rabbling mechanism, form multizone fluid circulation, messenger's feed liquid distributes evenly, has increased the heat -transfer surface, has improved heat exchange efficiency. And the concentrated jar of evacuation effect through the vacuum pump keeps negative pressure, the temperature that can reduce the concentration process is distilled to the negative pressure, shortens concentration time, improves production efficiency.
Description
Technical field
This utility model relates to a kind of bile acid enrichment facility.
Background technology
Bile acid adds to as endogenous emulsifying agent can improve broiler carcass quality in feedstuff, so in recent years
Carry out the application in aquaculture more and more extensive.In bile acid production technology, obtain after Pulvis Fellis Suis saponification
Saponification product concentration tank to be sent to after decolouring, be acidified, extracting concentrates, and is dried after concentration again, final
To bile acid product.At enrichment process, the way that traditional handicraft is taked is to concentrate with steam heating at ambient pressure
Extract in tank, makes extract seethe with excitement after reaching boiling point, and the steam that boiling produces imports condenser through pipeline
Middle condensation separation, and the continuous distillation and concentration of extract in concentration tank, finally give solid product.This dense
Contracting equipment is owing to using air-distillation, and evaporating temperature is high, and concentration time is long, causes production efficiency low.
Utility model content
This utility model is in order to make up the deficiencies in the prior art, it is provided that a kind of reasonable in design, reduction concentration temperature
Degree, improve thickening efficiency, time saving and energy saving bile acid enrichment facility, solve and ask present in prior art
Topic.
This utility model is achieved by the following technical solution:
A kind of bile acid enrichment facility, including concentration tank, condenser and liquid collecting tank, sets at the top of concentration tank
Having a concentration tank charging aperture, the bottom side at concentration tank is provided with a concentration tank discharging opening, concentration tank charging aperture
Inner side be connected with a nebulizer, the outer sheath at concentration tank is provided with a chuck, in top and the bottom of chuck
It is respectively equipped with a chuck medium entrance and a chuck media outlet on sidewall, is located at the dense of concentration tank top side
Contracting tank steam (vapor) outlet separates two-way by pipeline after a vacuum pump, and a road is connected with chuck medium entrance,
Another road is connected with the charging aperture of condenser, chuck media outlet by pipeline also with the charging aperture of condenser
Being connected, the discharging opening of condenser is connected with the charging aperture of liquid collecting tank through a condensed fluid delivery pump by pipeline,
Lower inside at concentration tank is provided with a rabbling mechanism.
Described rabbling mechanism includes the shaft being located at concentration tank bottom, and the bottom of described shaft is from concentration
The bottom of tank is connected with the output shaft of a motor after passing, and is provided with a stirring ribbon on shaft, in stirring
Be provided with outside ribbon one encirclement stirring ribbon guide shell, the bottom of guide shell by some connecting rods with stir
Mix axle to be connected.
A heater it is provided with on pipeline between vacuum pump and chuck medium entrance.
The beneficial effects of the utility model are: this bile acid enrichment facility, make extraction by the stirring of rabbling mechanism
Taking liquid at concentration tank internal circulation flow, shaft is positioned at the bottom of concentration tank, and by the motor bottom concentration tank
Drive, the good stability of shaft.Stirring ribbon coordinates guide shell, forms the circulation of multizone fluid, makes material
Liquid is evenly distributed, and increases heat-transfer surface, improves heat exchange efficiency.Further, concentration tank taking out by vacuum pump
Vacuum action keeps negative pressure state, and vacuum distillation can reduce the temperature of concentration process, shortens concentration time, carries
High efficiency.
Accompanying drawing explanation
Below in conjunction with the accompanying drawings this utility model is further described.
Fig. 1 is structural representation of the present utility model.
In figure, 1, concentration tank, 2, condenser, 3, liquid collecting tank, 4, concentration tank charging aperture, 5, concentration tank
Discharging opening, 6, nebulizer, 7, chuck, 8, chuck medium entrance, 9, chuck media outlet, 10, dense
Contracting tank steam (vapor) outlet, 11, vacuum pump, 12, condensed fluid delivery pump, 13, shaft, 14, motor, 15,
Stirring ribbon, 16, guide shell, 17, connecting rod, 18, heater.
Detailed description of the invention
For the technical characterstic of this programme can be clearly described, below by detailed description of the invention, and combine its accompanying drawing,
The utility model is elaborated.
As shown in fig. 1, this embodiment includes concentration tank 1, condenser 2 and liquid collecting tank 3, at concentration tank 1
Top be provided with a concentration tank charging aperture 4, the bottom side at concentration tank 1 is provided with a concentration tank discharging opening 5,
Concentration tank feeds the inner side of 4 mouthfuls and is connected with a nebulizer 6, and the outer sheath at concentration tank 1 is provided with a chuck 7,
The top and lower sides of chuck 7 are respectively equipped with chuck medium entrance 8 and a chuck media outlet 9,
The concentration tank steam (vapor) outlet 10 being located at concentration tank 1 top side separates two by pipeline after a vacuum pump 11
Road, a road is connected with chuck medium entrance 8, and another road is connected with the charging aperture of condenser 2, chuck
Media outlet 9 by pipeline also charging aperture with condenser 2 be connected, the discharging opening of condenser 2 is by pipe
Road one condensed fluid delivery pump 12 is connected with the charging aperture of liquid collecting tank 3, and the lower inside at concentration tank 1 sets
There is a rabbling mechanism.
Described rabbling mechanism includes the shaft 13 being located at concentration tank 1 bottom, the bottom of described shaft 13
After the bottom of concentration tank 1 passes, the output shaft with a motor 14 is connected, and is provided with one and stirs on shaft 13
Mix ribbon 15, outside stirring ribbon 15, be provided with the guide shell 16 of an encirclement stirring ribbon 15, guide shell 16
Bottom be connected with shaft 13 by some connecting rods 17.
A heater 18 it is provided with on pipeline between vacuum pump 11 and chuck medium entrance 8.
During production, the saponification product that Pulvis Fellis Suis obtains after saponification tank saponification pass through after decolouring, be acidified, extracting
Concentration tank charging aperture 4 enters concentration tank 1 after nebulizer 6 is atomized, and in concentration tank 1, extract is through chuck 7
In steam ebuillition of heated, boiling produce steam through vacuum pump 11 extract out one tunnel enter chuck 7, a road is entered
Enter condenser 2.Steam is absorbed after heat also into condenser 2, at condenser 2 through later from chuck 7
In, after two-way steam is condensed into liquid, condensed liquid delivery pump 12 is delivered to liquid collecting tank 3.Concentration tank 1
The interior continuous distillation and concentration of extract, finally gives solid product and discharges from concentration tank discharging opening 5.By stirring
The stirring mixing mechanism makes extract be positioned at the bottom of concentration tank 1 at concentration tank 1 internal circulation flow, shaft 13,
And driven by the motor 14 bottom concentration tank 1, the good stability of shaft 13.Stirring ribbon 15 coordinates leads
Flow cartridge 16, forms the circulation of multizone fluid, makes feed liquid be evenly distributed, increase heat-transfer surface, improve heat exchange
Efficiency.Further, concentration tank 1 keeps negative pressure state by the vacuum action of vacuum pump 11, and vacuum distillation can
Reduce the temperature of concentration process, shorten concentration time, improve production efficiency.
This utility model does not describes part in detail, is the known technology of those skilled in the art of the present technique.Finally illustrate
, above example is only in order to illustrate the technical solution of the utility model and unrestricted, although with reference to preferably
This utility model has been described in detail by embodiment, it will be understood by those within the art that, permissible
The technical solution of the utility model is modified or equivalent, without deviating from this utility model technical side
The objective of case and scope, it all should be contained in the middle of right of the present utility model.
Claims (3)
1. a bile acid enrichment facility, is characterized in that: include concentration tank, condenser and liquid collecting tank, dense
The top of contracting tank is provided with a concentration tank charging aperture, and the bottom side at concentration tank is provided with a concentration tank discharging opening,
The inner side of concentration tank charging aperture is connected with a nebulizer, and the outer sheath at concentration tank is provided with a chuck, at chuck
Top and lower sides on be respectively equipped with a chuck medium entrance and a chuck media outlet, be located at concentration tank
The concentration tank steam (vapor) outlet of top side separates two-way by pipeline after a vacuum pump, a road and chuck medium
Import is connected, and another road is connected with the charging aperture of condenser, and chuck media outlet passes through pipeline also with cold
The charging aperture of condenser is connected, and the discharging opening of condenser passes through pipeline through a condensed fluid delivery pump and liquid collecting tank
Charging aperture is connected, and the lower inside at concentration tank is provided with a rabbling mechanism.
A kind of bile acid enrichment facility the most according to claim 1, is characterized in that: described rabbling mechanism
Including being located at a shaft of concentration tank bottom, the bottom of described shaft pass from the bottom of concentration tank after with
The output shaft of one motor is connected, and is provided with a stirring ribbon on shaft, is provided with a bag outside stirring ribbon
Enclosing the guide shell of stirring ribbon, the bottom of guide shell is connected with shaft by some connecting rods.
A kind of bile acid enrichment facility the most according to claim 1, is characterized in that: at vacuum pump and folder
Pipeline between set medium entrance is provided with a heater.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620269403.0U CN205549639U (en) | 2016-03-31 | 2016-03-31 | Bile acid enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620269403.0U CN205549639U (en) | 2016-03-31 | 2016-03-31 | Bile acid enrichment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205549639U true CN205549639U (en) | 2016-09-07 |
Family
ID=56812735
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620269403.0U Active CN205549639U (en) | 2016-03-31 | 2016-03-31 | Bile acid enrichment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205549639U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110327639A (en) * | 2019-06-28 | 2019-10-15 | 中鸿纳米纤维技术丹阳有限公司 | A kind of nano-cellulose polymer composites drying equipment |
| CN114098009A (en) * | 2021-11-22 | 2022-03-01 | 常德云港生物科技有限公司 | Preparation facilities of pig gall powder after pig gall draws bilirubin |
-
2016
- 2016-03-31 CN CN201620269403.0U patent/CN205549639U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110327639A (en) * | 2019-06-28 | 2019-10-15 | 中鸿纳米纤维技术丹阳有限公司 | A kind of nano-cellulose polymer composites drying equipment |
| CN114098009A (en) * | 2021-11-22 | 2022-03-01 | 常德云港生物科技有限公司 | Preparation facilities of pig gall powder after pig gall draws bilirubin |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204656056U (en) | A kind of tasteless Chinese medicine extracting tank | |
| CN202359093U (en) | Plant essential oil extraction device | |
| CN208553176U (en) | A kind of chemical industry distilling apparatus | |
| CN205549639U (en) | Bile acid enrichment facility | |
| CN211169934U (en) | Miniature evaporation crystallization equipment | |
| CN201300008Y (en) | Oil filter system for reclaiming waste oil | |
| CN108408812B (en) | Desalination method and device for salt-containing wastewater | |
| CN110669590A (en) | System and method for continuously producing fatty acid by soapstock | |
| CN103301641B (en) | Reduced pressure and evaporation concentrator capable of circularly utilizing heat energy | |
| CN206676023U (en) | A kind of traditional Chinese medicine extraction separator | |
| CN209270849U (en) | A kind of vacuum concentration evaporator | |
| CN104761009A (en) | Industrial waste water processing system | |
| CN103977579B (en) | Ratio concentration and evaporation device | |
| CN206315513U (en) | A kind of new oily-water seperating equipment | |
| CN206396157U (en) | A kind of perfume purifies distilling apparatus | |
| CN107337707A (en) | A kind of drying enrichment facility of high efficiency extraction Fish protein | |
| CN101537260B (en) | Evaporation method by use of turbine compression fan | |
| CN205182207U (en) | Continuous vacuum dehydration of falling liquid film formula or dealcoholize device | |
| CN209522606U (en) | A kind of evaporator system | |
| CN210251245U (en) | A vacuum concentrator for ganoderan | |
| CN208907094U (en) | A kind of device crystallized for antibacterial peptide with dissolution | |
| CN208770862U (en) | Interior heat cycles vaporising device and vapo(u)rization system | |
| CN102442884B (en) | Method for recovering ethanol during soy production process and device thereof | |
| CN206051896U (en) | A kind of soybean phospholipid extraction element | |
| CN203842346U (en) | Spiral and annular two-stage series-connection type gutta-percha leaching device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: No. 9 Yanying North Road, Yanbei Street Office, Qihe County, Dezhou City, Shandong Province, 253000 Patentee after: Shandong Longchang Animal Health Products Co.,Ltd. Address before: No. 1 North Park Road, Qihe Economic Development Zone, Qihe County, Dezhou City, Shandong Province, 251100 Patentee before: SHANDONG LONGCHANG ANIMAL HEALTH PRODUCT Co.,Ltd. |
|
| CP03 | Change of name, title or address |