CN202157060U - Grease molecular distiller - Google Patents
Grease molecular distiller Download PDFInfo
- Publication number
- CN202157060U CN202157060U CN2011202527336U CN201120252733U CN202157060U CN 202157060 U CN202157060 U CN 202157060U CN 2011202527336 U CN2011202527336 U CN 2011202527336U CN 201120252733 U CN201120252733 U CN 201120252733U CN 202157060 U CN202157060 U CN 202157060U
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- CN
- China
- Prior art keywords
- chamber
- grease
- oil
- heat
- depickling
- 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
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- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The utility model discloses a grease molecular distiller belonging to a grease physical refining and depickling apparatus. The grease molecular distiller overcomes the defects of high cost, inconvenient equipment installation, non-ideal depickling effect and energy resource waste of the traditional grease physical refining and depickling way in the prior art. The grease molecular distiller mainly comprises an oil chamber and a heat-conduction oil chamber, wherein the oil chamber is provided with a chamber A and a chamber B; a coarse oil inlet is arranged on the upper part of the chamber A; a finished oil outlet is arranged on the lower part of the chamber B; and the heat-conduction oil chamber is provided with a heat-conduction oil inlet and a heat-conduction oil outlet. The grease molecular distiller is mainly used in the grease physical refining depickling technology.
Description
Technical field
The utility model belongs to grease physical refining deacidification field, specifically, relates in particular to a kind of grease molecular still.
Background technology
The material filling type extracting tower that conventional grease physical refining deacidification mode adopts, cost is high, the equipment mounting height need be higher than 11 meters, if the multitower combination uses, factory building height will be more than 20 meters, and deacidification effect is undesirable.Secondly the extracting tower oil-feed needs heating in advance; Promptly earlier oil is heated to 260 degree and gets into extracting tower again; In the process of depickling, because a large amount of heats are taken away in the lipid acid vaporization the interior temperature of tower is sharply descended, influenced deacidification effect greatly; And extracting tower could get into following one deodorization procedures after must heating once more, wasted the energy.
Summary of the invention
In order to solve conventional grease physical refining deacidification mode in the prior art, cost is high, equipment is installed inconvenience, and deacidification effect is undesirable, the defective that wastes energy, and the utility model provides a kind of grease molecular still.
The utility model is to adopt following technical scheme to realize:
A kind of grease molecular still comprises oil pocket, heat conduction grease chamber, and said oil pocket is provided with chamber first, chamber second, and top, the export of finished oil that the crude oil import is positioned at the chamber first is positioned at the bottom of chamber second; Said heat conduction grease chamber is provided with heat conductive oil inlet, thermal oil outlet.
Compared with prior art, the beneficial effect of the utility model is: utilize the short-path distillation principle, only need increase the length of equipment according to output, no longer need 20 meters high factory buildings, reduced the cost of founding the factory; But owing to use the thermal oil direct heating, make that oily temperature does not descend in the whole machining process process, forms good deacidification effect, subsequent processing deodorization simultaneously is additional heat may no longer, has played saving cost, energy-conservation effect.
Description of drawings
Fig. 1 is the front view of the utility model;
Fig. 2 is the vertical view of the utility model.
Chamber second in the drawings, 1; 2, oil pocket; 3, heat conduction grease chamber; 4, vacuum port; 5, crude oil import; 6, chamber first; 7, thermal oil outlet; 8, heat conductive oil inlet; 9, export of finished oil.
Embodiment
Below in conjunction with accompanying drawing the utility model is described further:
A kind of grease molecular still comprises oil pocket 2, heat conduction grease chamber 3, and said oil pocket 2 is provided with chamber first 6, chamber second 1, and crude oil import 5 is positioned at the top of chamber first 6, the bottom that export of finished oil 9 is positioned at chamber second 1; Said heat conduction grease chamber 3 is provided with heat conductive oil inlet 8, thermal oil outlet 7.
The utility model is raised the crude oil entrance end when mounted, makes entire equipment be inclined to 30 degree angles.Vacuum port 4 connects vacuum system; Crude oil import 5 connects the crude oil pump, to the equipment fuel feeding; Export of finished oil 9 is connected to down deodorization procedures one; Heat conductive oil inlet 8 connects the thermal oil feedway; Thermal oil outlet 9 connects the thermal oil retrieving arrangement.Be provided with process furnace between thermal oil feedway and the thermal oil retrieving arrangement, make thermal oil form the loop in the course of the work.
The utility model vacuumizes through vacuum port 4 in use, makes oil pocket 2 be in high vacuum state; Through process furnace is heated, and thermal oil is squeezed into heat conduction grease chamber 3, thereby control oil pocket 2 is in the 260 degree conditions of high temperature; At this moment, crude oil to be processed gets into from crude oil import 5, when the chamber first 6 below oil is filled crude oil import 5; Because the effect of device inclined, gravity, crude oil forms the very thin oil film of one deck through oil pocket 2 and flows to 1 li of chamber second, flows into subsequent processing through export of finished oil 9 again; In this process, since the relation of temperature and vacuum, the free fatty acids vaporization in the crude oil; Taken away through vacuum port 5, accomplished the short-path distillation deacidification.
Claims (1)
1. grease molecular still; Comprise oil pocket (2), heat conduction grease chamber (3); It is characterized in that: said oil pocket (2) is provided with chamber first (6), chamber second (1), and crude oil import (5) is positioned at the top of chamber first (6), the bottom that export of finished oil (9) is positioned at chamber second (1); Said heat conduction grease chamber (3) is provided with heat conductive oil inlet (8), thermal oil outlet (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202527336U CN202157060U (en) | 2011-07-18 | 2011-07-18 | Grease molecular distiller |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202527336U CN202157060U (en) | 2011-07-18 | 2011-07-18 | Grease molecular distiller |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202157060U true CN202157060U (en) | 2012-03-07 |
Family
ID=45764702
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011202527336U Expired - Fee Related CN202157060U (en) | 2011-07-18 | 2011-07-18 | Grease molecular distiller |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202157060U (en) |
-
2011
- 2011-07-18 CN CN2011202527336U patent/CN202157060U/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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120307 Termination date: 20140718 |
|
| EXPY | Termination of patent right or utility model |