CN202989095U - Heat exchange system for soybean oil refining - Google Patents
Heat exchange system for soybean oil refining Download PDFInfo
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- CN202989095U CN202989095U CN 201320004226 CN201320004226U CN202989095U CN 202989095 U CN202989095 U CN 202989095U CN 201320004226 CN201320004226 CN 201320004226 CN 201320004226 U CN201320004226 U CN 201320004226U CN 202989095 U CN202989095 U CN 202989095U
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- heat exchanger
- exchange system
- heat
- heat exchange
- condenser
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Abstract
The utility model discloses a heat exchange system for soybean oil refining. The system comprises a heat exchanger connected with a centrifugal machine and a heater connected with the heat exchanger, wherein the heat exchanger is connected with a deodorization pot; the heat exchange system also comprises a condenser connected with the heat exchanger; the condenser is connected with a product oil tank; and the deodorization pot is also connected with the heat exchanger. According to the heat exchange system disclosed by the utility model, the heat exchanger absorbs the heat released by oils in a condensation process, and the energy is effectively utilized again; a tubular heat exchanger has longer service life than a plate heat exchanger adopted in the traditional technology, thus the maintenance cost is obviously lowered; the need for cooling oils can be met simply by mounting one condenser in the system; and the heat exchange system disclosed by the utility model has the advantages of simple structure, high heat exchange efficiency, low maintenance cost and energy conservation.
Description
Technical field
The utility model relates to the edible fat production technical field, especially relates to a kind of soya-bean oil refining heat-exchange system.
Background technology
In soya-bean oil when refining, need to be increased to 150 ℃ from 80 ℃ with the grease temperature, and the temperature of refining complete rear processed oil needs be cooled at least below 80 ℃ and can put in storage from 150 ℃.In prior art, grease need to pass into a large amount of water vapour when heating up, utilize steam to heat, during cooling, use plate-type condenser to the processed oil condensation of lowering the temperature, there is following shortcoming in this mode: 1) intensification and temperature-fall period all carry out separately, and the energy that discharges in temperature-fall period can't recycle, and has caused the waste of the energy; 2) owing to entering into plate-type condenser oil product excess Temperature, the life-span of heat exchange mat in condenser is significantly shortened in the cooling condensation meeting of carrying out under high temperature, thereby has increased the condenser maintenance cost.
Summary of the invention
The purpose of this utility model is to overcome the shortcoming that exists in prior art, provide a kind of energy can cycling and reutilization, the soya-bean oil refining heat-exchange system of with low cost, long service life, this system has good heat transfer effect, the technical scheme that adopts is: a kind of soya-bean oil refining heat-exchange system, it is characterized in that: described heat-exchange system comprises the interchanger that is connected with whizzer and the well heater that is connected with described interchanger, and described interchanger is connected with odor removing pot; Described heat-exchange system also comprises the condenser that is connected with interchanger, and described condenser is connected with product tank; Described odor removing pot also is connected with described interchanger.
Technical characterictic of the present utility model also has: described interchanger is tubular heat exchanger.
The beneficial effects of the utility model are: the interchanger in native system has absorbed the heat that in the condensation process, oil product discharges, and with this Energy Efficient reapplication; The plate-type heat exchanger that tubular heat exchanger uses in the conventional art has longer work-ing life, thereby has significantly reduced maintenance cost; Only need to install a condenser in native system and can satisfy oil product cooling demand, the utlity model has simple in structure, heat exchange efficiency is high, maintenance cost is low, the advantage of saving the energy.
Description of drawings
Accompanying drawing 1 is the utility model structural representation, and wherein 1 is whizzer, the 2nd, and interchanger, the 3rd, well heater, the 4th, odor removing pot, the 5th, condenser, the 6th, product tank.
Embodiment
Below in conjunction with accompanying drawing, embodiment of the present utility model is described.The utility model discloses a kind of soya-bean oil refining heat-exchange system, this heat-exchange system comprises the interchanger 2 that is connected with whizzer 1, the well heater 3 that is connected with interchanger 2 and condenser 5, interchanger 2 is connected with odor removing pot 4, and condenser 5 is connected with product tank 6, and odor removing pot 4 also is connected with interchanger 2.In order to realize better heat transfer effect, this interchanger 2 has adopted that heat exchange efficiency is high, the tubular heat exchanger of long service life.
need at first the grease of exporting from whizzer 1 to be heated up in oil and fat refining, temperature-rise period is: from the grease temperature of whizzer 1 output 80 ℃ of left and right, at first this grease delivers in interchanger 2, after being elevated to 115 ℃, the temperature of grease is transported to well heater 3 relaying temperature of continuing rising from interchanger 2, the heating agent of well heater 3 is steam, after being raised to 150 ℃, its temperature enters into odor removing pot 4 deodorizing, and the complete processed oil that obtains of deodorizing needed cooling before entering product tank 6, the process of cooling is: at first the processed oil of output is transported in interchanger 2 from odor removing pot 4, enter into condenser 5 and continue cooling when its temperature drops to 110 ℃ of left and right, until temperature is reduced to below 80 ℃, processed oil enters into product tank, refining machines.
Certainly; above-mentioned explanation is not limitation of the utility model; the utility model also is not limited only to above-mentioned giving an example, and the variation that those skilled in the art make in essential scope of the present utility model, remodeling, interpolation or replacement also belong to protection domain of the present utility model.
Claims (2)
1. soya-bean oil refining heat-exchange system, it is characterized in that: described heat-exchange system comprises the interchanger that is connected with whizzer and the well heater that is connected with described interchanger, and described interchanger is connected with odor removing pot; Described heat-exchange system also comprises the condenser that is connected with interchanger, and described condenser is connected with product tank; Described odor removing pot also is connected with described interchanger.
2. according to soya-bean oil refining heat-exchange system claimed in claim 1, it is characterized in that: described interchanger is tubular heat exchanger.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320004226 CN202989095U (en) | 2013-01-06 | 2013-01-06 | Heat exchange system for soybean oil refining |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320004226 CN202989095U (en) | 2013-01-06 | 2013-01-06 | Heat exchange system for soybean oil refining |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202989095U true CN202989095U (en) | 2013-06-12 |
Family
ID=48560292
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320004226 Expired - Fee Related CN202989095U (en) | 2013-01-06 | 2013-01-06 | Heat exchange system for soybean oil refining |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202989095U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105154224A (en) * | 2015-09-14 | 2015-12-16 | 濮阳市广源油脂有限公司 | Device and method for recovering heat in oil and fat refining process |
| CN107937129A (en) * | 2017-11-15 | 2018-04-20 | 广汉市航佳食品有限公司 | Temperature-controlling system and technique in a kind of edible animal grease refining process |
-
2013
- 2013-01-06 CN CN 201320004226 patent/CN202989095U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105154224A (en) * | 2015-09-14 | 2015-12-16 | 濮阳市广源油脂有限公司 | Device and method for recovering heat in oil and fat refining process |
| CN105154224B (en) * | 2015-09-14 | 2019-06-11 | 濮阳市广源油脂有限公司 | Heat reclaim unit and recovery method in a kind of oil and fat refining process |
| CN107937129A (en) * | 2017-11-15 | 2018-04-20 | 广汉市航佳食品有限公司 | Temperature-controlling system and technique in a kind of edible animal grease refining process |
| CN107937129B (en) * | 2017-11-15 | 2021-03-23 | 四川航佳生物科技有限公司 | Temperature control system and process in edible animal oil and fat refining process |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130612 Termination date: 20140106 |