CN204509242U - Oil-oily heat exchange treatment facility - Google Patents
Oil-oily heat exchange treatment facility Download PDFInfo
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- CN204509242U CN204509242U CN201520069238.XU CN201520069238U CN204509242U CN 204509242 U CN204509242 U CN 204509242U CN 201520069238 U CN201520069238 U CN 201520069238U CN 204509242 U CN204509242 U CN 204509242U
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- interchanger
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Abstract
The utility model provides a kind of oil-oily heat exchange treatment facility, primarily of interchanger and hotline heater composition, treat deodorised oil interchanger I, treat deodorised oil interchanger II, hotline heater I is connected successively with deodorizing tower, deodorizing tower successively with treat deodorised oil interchanger II and treat that deodorised oil interchanger I branch road is connected; Treat deodorised oil interchanger I successively with treat that precipitation oil heat exchanger, type crude oil heat exchanger and water cooler are connected; Treat that precipitation oil heat exchanger branch road is connected with hotline heater II and precipitation tower successively; Treat that precipitation oil heat exchanger is directly connected with precipitation tower by another branch road; Type crude oil heat exchanger branch road is connected with hotline heater III, oily alkali reaction device successively; Type crude oil heat exchanger is directly connected with oily alkali reaction device by another branch road.Adopting the utility model, utilizing the waste heat of deodorised oil to treating the heating of precipitation oil wool lubricant, can also subtract deodorised oil cooling burden, save energy simultaneously.
Description
Technical field
The utility model relates to a kind of oil-oily heat exchange treatment facility.
Background technology
Existing oil product equipment for Heating Processing is all independent operating, such as, treats deodorised oil first after two interchanger, a hotline heater heating, enters deodorizing tower; After completing deodorization, extract out again after two interchanger by deodorizing tower, oil temperature is down to about 140 DEG C, and to water cooler cooling, oil temperature is down to about 45 DEG C, is deodorization processed oil.Crude oil is after a hotline heater heating, and temperature reaches about 65 DEG C, enters oily alkali reaction tower.And treat that precipitation oil is after a hotline heater heating, oil temperature reaches about 110 DEG C, enters precipitation tower.The heat treatment process of different oil product operates separately, both adds equipment cost, and wastes mass energy again.
Summary of the invention
The purpose of this utility model is to provide a kind of oil-oily heat exchange treatment facility, to solve the problems of the technologies described above.
The utility model is primarily of interchanger and hotline heater composition, solving the technical scheme that its problem adopts is, treat deodorised oil interchanger I, treat deodorised oil interchanger II, hotline heater I is connected successively with deodorizing tower, deodorizing tower successively with treat deodorised oil interchanger II and treat that deodorised oil interchanger I branch road is connected; Treat deodorised oil interchanger I successively with treat that precipitation oil heat exchanger, type crude oil heat exchanger and water cooler are connected; Treat that precipitation oil heat exchanger branch road is connected with hotline heater II and precipitation tower successively; Treat that precipitation oil heat exchanger is directly connected with precipitation tower by another branch road; Type crude oil heat exchanger branch road is connected with hotline heater III, oily alkali reaction device successively; Type crude oil heat exchanger is directly connected with oily alkali reaction device by another branch road.
Adopting the utility model, utilizing the waste heat of deodorised oil to treating the heating of precipitation oil wool lubricant, can also subtract deodorised oil cooling burden, save energy simultaneously.
Accompanying drawing explanation
Above-mentioned and/or additional aspect of the present utility model and advantage will become obvious and easy understand from the following description of the accompanying drawings of embodiments, wherein:
Fig. 1 is structural representation of the present utility model.
Embodiment
Be described below in detail embodiment of the present utility model, described embodiment is exemplary, only for explaining the utility model, and can not be interpreted as restriction of the present utility model.
As shown in the figure, treat deodorised oil interchanger I, treat deodorised oil interchanger II, hotline heater I is connected successively with deodorizing tower, deodorizing tower successively with treat deodorised oil interchanger II and treat that deodorised oil interchanger I branch road is connected; Treat deodorised oil interchanger I successively with treat that precipitation oil heat exchanger, type crude oil heat exchanger and water cooler are connected; Treat that precipitation oil heat exchanger branch road is connected with hotline heater II and precipitation tower successively; Treat that precipitation oil heat exchanger is directly connected with precipitation tower by another branch road; Type crude oil heat exchanger branch road is connected with hotline heater III, oily alkali reaction device successively; Type crude oil heat exchanger is directly connected with oily alkali reaction device by another branch road, and all pipelines all arrange valve.
During use, treat deodorised oil first after treating deodorised oil interchanger I, treating deodorised oil interchanger II and hotline heater I, enter deodorizing tower.After deodorization completes, extracted out by deodorizing tower, again after treating deodorised oil interchanger II and treating deodorised oil interchanger I, oil temperature is down to about 140 DEG C, then through treating precipitation oil heat exchanger and treating the heat exchange of precipitation oil, oil temperature is down to about 100 DEG C and is treated that precipitation oil oil temperature reaches more than 100 DEG C simultaneously, directly enters precipitation tower precipitation; If do not reach precipitation temperature, then carry out precipitation after hotline heater II heats.Deodorised oil, through after precipitation oil heat exchanger, enters type crude oil heat exchanger and crude oil carries out heat exchange, and oil temperature is down to about 60 DEG C; Meanwhile, crude oil oil temperature reaches more than 60 DEG C, directly enters oily alkali reaction device and processes; If crude oil temperature does not reach processing requirement, then heat laggard row relax by hotline heater III.Through the deodorised oil of type crude oil heat exchanger after water cooler slightly cools, be deodorization processed oil.Adopt the utility model, both make use of the remaining temperature of deodorised oil, additionally reduce processed oil cooling burden, utilize warm heat exchange more than deodorised oil can save lump coal about 40%, cooling power saves 4Kw/ ton, reduces crude oil tooling cost 5-7 yuan/ton.
Although illustrate and described embodiment of the present utility model, for the ordinary skill in the art, be appreciated that and can carry out multiple change, amendment, replacement and modification to these embodiments when not departing from principle of the present utility model and spirit, scope of the present utility model is by claims and equivalents thereof.
Claims (1)
1. oil-oily heat exchange treatment facility, it is characterized in that, primarily of interchanger and hotline heater composition, treat deodorised oil interchanger I, treat deodorised oil interchanger II, hotline heater I is connected successively with deodorizing tower, deodorizing tower successively with treat deodorised oil interchanger II and treat that deodorised oil interchanger I branch road is connected; Treat deodorised oil interchanger I successively with treat that precipitation oil heat exchanger, type crude oil heat exchanger and water cooler are connected; Treat that precipitation oil heat exchanger branch road is connected with hotline heater II and precipitation tower successively; Treat that precipitation oil heat exchanger is directly connected with precipitation tower by another branch road; Type crude oil heat exchanger branch road is connected with hotline heater III, oily alkali reaction device successively; Type crude oil heat exchanger is directly connected with oily alkali reaction device by another branch road.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520069238.XU CN204509242U (en) | 2015-02-02 | 2015-02-02 | Oil-oily heat exchange treatment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520069238.XU CN204509242U (en) | 2015-02-02 | 2015-02-02 | Oil-oily heat exchange treatment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204509242U true CN204509242U (en) | 2015-07-29 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520069238.XU Active CN204509242U (en) | 2015-02-02 | 2015-02-02 | Oil-oily heat exchange treatment facility |
Country Status (1)
| Country | Link |
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| CN (1) | CN204509242U (en) |
Cited By (1)
| 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 |
-
2015
- 2015-02-02 CN CN201520069238.XU patent/CN204509242U/en active Active
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 |
| 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 |
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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 | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160219 Address after: 253000 South Town Industrial Park, Xiajin County, Dezhou, Shandong Patentee after: Shandong clever wife Food Technology Co., Ltd. Address before: 253200 South Town Industrial Park, Xiajin County, Dezhou, Shandong Patentee before: Shandong Hengxing Grease Co.,Ltd. |