CN204307395U - Centrifugal molecular distillating system - Google Patents
Centrifugal molecular distillating system Download PDFInfo
- Publication number
- CN204307395U CN204307395U CN201420680681.6U CN201420680681U CN204307395U CN 204307395 U CN204307395 U CN 204307395U CN 201420680681 U CN201420680681 U CN 201420680681U CN 204307395 U CN204307395 U CN 204307395U
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- molecular
- centrifugal
- distillating
- oil
- centrifugal molecular
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- 238000007789 sealing Methods 0.000 claims abstract description 10
- 238000009792 diffusion process Methods 0.000 claims description 14
- 239000000463 material Substances 0.000 abstract description 24
- 238000000034 method Methods 0.000 abstract description 14
- 238000004332 deodorization Methods 0.000 abstract description 7
- 238000007670 refining Methods 0.000 abstract description 7
- 238000002156 mixing Methods 0.000 abstract description 6
- 238000000926 separation method Methods 0.000 abstract description 6
- 230000003068 static effect Effects 0.000 abstract description 6
- 238000000199 molecular distillation Methods 0.000 description 4
- 238000009834 vaporization Methods 0.000 description 3
- 230000008016 vaporization Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 230000007306 turnover Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Centrifugal Separators (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a kind of centrifugal molecular distillating system, belong to technical field of food machinery.Centrifugal molecular distillating system of the present utility model, mainly solve the technical problem of material easy heat damage in separation process, also solve the problem of material back-mixing and static and dynamic sealing in molecular clock process, be applicable to separating VE from oil and fat refining deodorization distillate completely, its structure is simple, easy and simple to handle, easy to use, applied widely.Centrifugal molecular distillating system of the present utility model, comprises centrifugal molecular distillator, described centrifugal molecular distillator is connected with feeding device, vacuum system and discharge system, and described vacuum system is connected with discharge system.
Description
Technical field
The utility model relates to technical field of food machinery, especially a kind of molecular distillation technique.
Background technology
In food-processing industry, sometimes need to extract another predetermined substance from certain material, such as separating VE from oil and fat refining deodorization distillate, need to adopt molecular distillation technique, also namely under vacuum, material is heated, gasifies, is separated within the extreme time, to reach the object of purification; But current molecular distillation technique falls behind, and cannot reach anticipation object; But current molecular distillation technique, exists the problems such as material back-mixing problem, static and dynamic sealing, and the easy heat damage of material.
Utility model content
Goal of the invention of the present utility model is: for above-mentioned Problems existing, a kind of centrifugal molecular distillating system is provided, mainly solve the technical problem of material easy heat damage in separation process, also solve the problem of material back-mixing and static and dynamic sealing in molecular clock process, be applicable to separating VE from oil and fat refining deodorization distillate completely, its structure is simple, easy and simple to handle, easy to use, applied widely.
The technical solution adopted in the utility model is as follows:
Centrifugal molecular distillating system of the present utility model, comprises centrifugal molecular distillator, described centrifugal molecular distillator is connected with feeding device, vacuum system and discharge system, and described vacuum system is connected with discharge system.
Due to said structure, by centrifugal molecular distillator, material is separated, then ensures normally carrying out of material through vacuum system; Discharge system is convenient to the eliminating of material; Centrifugal molecular distillating system of the present utility model, material easy heat damage in separation process can be avoided, also solve the problem of material back-mixing and static and dynamic sealing in molecular clock process, be applicable to separating VE from oil and fat refining deodorization distillate completely, its structure is simple, easy and simple to handle, easy to use, applied widely.
Centrifugal molecular distillating system of the present utility model, described centrifugal molecular distillator comprises molecular still body, described molecular still body is provided with heater and oil-sealing arrangement, the intrinsic centrifugal pressure of described molecular still is 0.133-1.33Pa, and the heat time of described heater is 0.05S.
Due to said structure, can be separated material, be applicable to separating VE from oil and fat refining deodorization distillate completely.
Centrifugal molecular distillating system of the present utility model, described feeding device includes head tank, feed pump and preheater, and described head tank is connected with feed pump, and described feed pump is connected with preheater, and described preheater is connected on molecular still body.
Due to said structure, be convenient to material to be sent in centrifugal molecular distillator be separated, be convenient to subsequent treatment.
Centrifugal molecular distillating system of the present utility model, described vacuum system comprises cold-trap, oil diffusion pump and oil circulating pump, described oil diffusion pump is connected on molecular still body by cold-trap one, described oil diffusion pump is connected with oil circulating pump one, described oil diffusion pump is parallel with oil circulating pump two, and described oil circulating pump one connects discharge system and head tank respectively by cold-trap two.
Due to said structure, in order to ensure that input and output material normally carries out, turnover batch can also must ensure the pressure identical with vaporization chamber.
Centrifugal molecular distillating system of the present utility model, described discharge system comprises being connected to molecular still body distillates tank and residue tank, described in distillate tank and be connected with cold-trap two; Described residue tank is connected with head tank.
Due to said structure, be convenient to the material after by separation and carry out division preservation.
In sum, owing to have employed technique scheme, the beneficial effects of the utility model are:
Centrifugal molecular distillating system of the present utility model, mainly solve the technical problem of material easy heat damage in separation process, also solve the problem of material back-mixing and static and dynamic sealing in molecular clock process, be applicable to separating VE from oil and fat refining deodorization distillate completely, its structure is simple, easy and simple to handle, easy to use, applied widely.
Accompanying drawing explanation
The utility model illustrates by example and with reference to the mode of accompanying drawing, wherein:
Fig. 1 is the schematic diagram of centrifugal molecular distillating system of the present utility model;
Mark in figure: 1-centrifugal molecular distillator, 2-heater, 3-oil-sealing arrangement, 4-preheater, 5-distillates tank, 6-feed pump, 7-head tank, 8-residue tank, and 9,10-cold-trap, 11-oil diffusion pump, 12,13-oil circulating pump, W-cooling water, S-steam.
Detailed description of the invention
All features disclosed in this description, or the step in disclosed all methods or process, except mutually exclusive feature and/or step, all can combine by any way.
Arbitrary feature disclosed in this description (comprising any accessory claim, summary), unless specifically stated otherwise, all can be replaced by other equivalences or the alternative features with similar object.That is, unless specifically stated otherwise, each feature is an example in a series of equivalence or similar characteristics.
As shown in Fig. 1, as shown in Figure 1, centrifugal molecular distillating system of the present utility model, comprise centrifugal molecular distillator 1, described centrifugal molecular distillator 1 comprises molecular still body, described molecular still body is provided with heater 2 and oil-sealing arrangement 3, and the intrinsic centrifugal pressure of described molecular still is 0.133-1.33Pa, and the heat time of described heater 2 is 0.05S; Described centrifugal molecular distillator 1 is connected with feeding device, vacuum system and discharge system, and described vacuum system is connected with discharge system.Wherein said feeding device includes head tank 7, feed pump 6 and preheater 4, and described head tank 7 is connected with feed pump 6, and described feed pump 6 is connected with preheater 4, and described preheater 4 is connected on molecular still body.Wherein said vacuum system comprises cold-trap, oil diffusion pump 11 and oil circulating pump, described oil diffusion pump 11 is connected on molecular still body by cold-trap one, described oil diffusion pump 11 is connected with oil circulating pump one, described oil diffusion pump 11 is parallel with oil circulating pump two, and described oil circulating pump one connects discharge system and head tank 7 respectively by cold-trap two.Wherein said discharge system comprises being connected to molecular still body distillates tank 5 and residue tank 8, described in distillate tank 5 and be connected with cold-trap two; Described residue tank 8 is connected with head tank 7.
Centrifugal molecular distillating system of the present utility model, its operation principle is: raw material is preheated to required temperature from head tank 7 through preheater 4 by feed pump 6, , pump into molecular still vaporization chamber rotating disk, material on rotating disk because the effect of centrifugal force forms the film of thickness 0.01-0.02, wherein the lower component of expense electricity to be evaporated rapidly with the effect of condition of high vacuum degree because being heated, and condensation on the cryosurface that rotating disk is parallel, enter distillate and distillate tank 5, boiling point comparatively great number component then enters fraction collection tank 8, and everything all completes within the extremely short time, because there is not material changes its performance problem because being heated, the component being difficult under making normal condition be separated is separated.The vacuum of vapo(u)rization system outstandingly turns pump 12 by oil, oil diffusion pump 11, cold-trap 9 complete, and in order to ensure that input and output material normally carries out, turnover batch can also must ensure the pressure identical with vaporization chamber, outstandingly turns pump 12 and 13, cold-trap 10 completes by oil.
Centrifugal molecular distillating system of the present utility model, mainly solve the technical problem of material easy heat damage in separation process, also solve the problem of material back-mixing and static and dynamic sealing in molecular clock process, be applicable to separating VE from oil and fat refining deodorization distillate completely, its structure is simple, easy and simple to handle, easy to use, applied widely.
The utility model is not limited to aforesaid detailed description of the invention.The utility model expands to any new feature of disclosing in this manual or any combination newly, and the step of the arbitrary new method disclosed or process or any combination newly.
Claims (5)
1. centrifugal molecular distillating system, is characterized in that: it comprises centrifugal molecular distillator (1), and (1) is connected with feeding device, vacuum system and discharge system to described centrifugal molecular distillator, and described vacuum system is connected with discharge system.
2. centrifugal molecular distillating system as claimed in claim 1, it is characterized in that: described centrifugal molecular distillator (1) comprises molecular still body, described molecular still body is provided with heater (2) and oil-sealing arrangement (3), the intrinsic centrifugal pressure of described molecular still is 0.133-1.33Pa, and the heat time of described heater (2) is 0.05S.
3. centrifugal molecular distillating system as claimed in claim 2, it is characterized in that: described feeding device includes head tank (7), feed pump (6) and preheater (4), described head tank (7) is connected with feed pump (6), described feed pump (6) is connected with preheater (4), and described preheater (4) is connected on molecular still body.
4. centrifugal molecular distillating system as claimed in claim 3, it is characterized in that: described vacuum system comprises cold-trap, oil diffusion pump (11) and oil circulating pump, described oil diffusion pump (11) is connected on molecular still body by cold-trap one, described oil diffusion pump (11) is connected with oil circulating pump one, described oil diffusion pump (11) is parallel with oil circulating pump two, and described oil circulating pump one connects discharge system and head tank (7) respectively by cold-trap two.
5. centrifugal molecular distillating system as claimed in claim 4, is characterized in that: described discharge system comprises being connected to molecular still body distillates tank (5) and residue tank (8), described in distillate tank (5) and be connected with cold-trap two; Described residue tank (8) is connected with head tank (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420680681.6U CN204307395U (en) | 2014-11-14 | 2014-11-14 | Centrifugal molecular distillating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420680681.6U CN204307395U (en) | 2014-11-14 | 2014-11-14 | Centrifugal molecular distillating system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204307395U true CN204307395U (en) | 2015-05-06 |
Family
ID=53129729
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420680681.6U Expired - Fee Related CN204307395U (en) | 2014-11-14 | 2014-11-14 | Centrifugal molecular distillating system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204307395U (en) |
-
2014
- 2014-11-14 CN CN201420680681.6U patent/CN204307395U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| CB03 | Change of inventor or designer information |
Inventor after: Fan Tirong Inventor before: Li Wei |
|
| COR | Change of bibliographic data | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160715 Address after: 336400 Jiangxi city of Yichun province Shanggao County Industrial Park gold heap function area Patentee after: JIANGXI CHANGHUI FOOD Co.,Ltd. Address before: Pengzhou City, Chengdu City, Sichuan province 610000 days Peng Building 1 No. 96 West Street Patentee before: CHENGDU CHUANGWEIKAI TECHNOLOGY INFORMATION CONSULTING Co.,Ltd. |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Centrifugal-type molecular distillation system Effective date of registration: 20180418 Granted publication date: 20150506 Pledgee: Jiangxi upper rural commercial bank Limited by Share Ltd. Pledgor: JIANGXI CHANGHUI FOOD Co.,Ltd. Registration number: 2018360000013 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150506 |