CN203582839U - Fatty acid methyl ester extracting device - Google Patents
Fatty acid methyl ester extracting device Download PDFInfo
- Publication number
- CN203582839U CN203582839U CN201320717387.3U CN201320717387U CN203582839U CN 203582839 U CN203582839 U CN 203582839U CN 201320717387 U CN201320717387 U CN 201320717387U CN 203582839 U CN203582839 U CN 203582839U
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- China
- Prior art keywords
- extracting
- pipeline
- methyl ester
- extraction tower
- fatty acid
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- Expired - Fee Related
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Fats And Perfumes (AREA)
- Extraction Or Liquid Replacement (AREA)
Abstract
The utility model provides a fatty acid methyl ester extracting device, and relates to a device which is used for extracting and separating an oil alcoholysis product in a fatty alcohol production process. The device is mainly used for solving the problems that in a conventional fatty alcohol production process, the device for extracting and separating the oil alcoholysis product is complicated to operate and high in energy consumption and installation cost, and a system is complicated. The fatty acid methyl ester extracting device comprises an extracting tower and an inversely U-shaped pipe, wherein a softening water feeding pipeline is arranged on the top of the extracting tower, a methyl ester discharging pipeline is arranged at the upper part of the extracting tower, a methyl ester and dry oil feeding pipeline is arranged at the lower part of the extracting tower, the bottom of the extracting tower is connected to a glycerin water pipeline, the glycerin water pipeline is connected to one end of the inversely U-shaped pipe, the other end of the glycerin water pipeline is connected to a glycerin water discharging pipeline, the middle of the top of the inversely U-shaped pipe is connected to a pressure-equalizing pipe, and the other end of the pressure-equalizing pipe is connected to the upper part of the extracting tower. The fatty acid methyl ester extracting device has the advantages of low installation cost, low energy consumption and simple operation.
Description
Technical field:
The utility model relates to a kind of device that grease alcoholysis product is carried out extracting and separating in producing fatty alcohol process.
Background technology:
On the extraction tower of the existing device that grease alcoholysis product is carried out extracting and separating in producing fatty alcohol process, be provided with interface table and Liquid level adjusting valve group, the separation interface height of the light constituent in extraction tower and heavy constituent need to be adjusted by variable valve group, complicated operation, system is lengthy and tedious, and big energy-consuming, installation cost is high.
Summary of the invention:
It is low that technical problem to be solved in the utility model is to provide a kind of installation cost, simple to operate, the fatty acid methyl ester extraction plant that consumes energy few.
Above-mentioned purpose is achieved in that it comprises extraction tower, softening water feeding line is arranged at extraction tower top, methyl esters discharging pipeline is arranged at extraction tower top, methyl esters and drier oil feeding line are arranged at extraction tower bottom, extraction tower bottom is connected with glycerol liquor pipeline, also comprise an inverted-loop tube, glycerol liquor pipeline is connected with one end of inverted-loop tube, the other end of inverted U-shaped pipeline is connected with glycerol liquor discharging pipeline, in the middle of the napex of inverted-loop tube, be connected with pressure equalizing pipe, the other end of pressure equalizing pipe is connected to the top of extraction tower.
The utility model has the advantages that: pass through calculation formula: the separation interface of methyl esters and glycerol liquor arrives the density of the height * methyl esters between methyl esters discharge nozzle: the separation interface of methyl esters and glycerol liquor and the density of the height * glycerol liquor between inverted-loop tube.So the separation interface height of methyl esters and glycerol liquor is fixed in extraction tower, saved the process of originally adjusting by variable valve group, can also utilize material self potential energy that the discharging power of heavy constituent is provided simultaneously.In addition, this device installation cost is low, and power consumption is few, simple to operate.
Accompanying drawing explanation:
Accompanying drawing is structural representation of the present utility model.
Embodiment:
With reference to accompanying drawing, it comprises extraction tower 1, softening water feeding line 2 is arranged at extraction tower top, and methyl esters discharging pipeline 4 is arranged at extraction tower top, and methyl esters and drier oil feeding line 8 are arranged at extraction tower bottom, extraction tower bottom is connected with glycerol liquor pipeline 7, also comprise an inverted-loop tube 5, glycerol liquor pipeline is connected with one end of inverted-loop tube, and the other end of inverted U-shaped pipeline is connected with glycerol liquor discharging pipeline 6, the crown center of inverted-loop tube is connected with pressure equalizing pipe 3, and the other end of pressure equalizing pipe is connected to the top of extraction tower.
Claims (1)
1. a fatty acid methyl ester extraction plant, comprise extraction tower (1), softening water feeding line (2) is arranged at extraction tower top, methyl esters discharging pipeline (4) is arranged at extraction tower top, methyl esters and drier oil feeding line (8) are arranged at extraction tower bottom, extraction tower bottom is connected with glycerol liquor pipeline (7), it is characterized in that: also comprise an inverted-loop tube (5), glycerol liquor pipeline is connected with one end of inverted-loop tube, the other end of inverted U-shaped pipeline is connected with glycerol liquor discharging pipeline (6), in the middle of the napex of inverted-loop tube, be connected with pressure equalizing pipe (3), the other end of pressure equalizing pipe is connected to the top of extraction tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320717387.3U CN203582839U (en) | 2013-11-07 | 2013-11-07 | Fatty acid methyl ester extracting device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320717387.3U CN203582839U (en) | 2013-11-07 | 2013-11-07 | Fatty acid methyl ester extracting device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203582839U true CN203582839U (en) | 2014-05-07 |
Family
ID=50580786
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320717387.3U Expired - Fee Related CN203582839U (en) | 2013-11-07 | 2013-11-07 | Fatty acid methyl ester extracting device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203582839U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113117375A (en) * | 2019-12-30 | 2021-07-16 | 湖北江田精密化学有限公司 | Extraction separation device |
-
2013
- 2013-11-07 CN CN201320717387.3U patent/CN203582839U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113117375A (en) * | 2019-12-30 | 2021-07-16 | 湖北江田精密化学有限公司 | Extraction separation device |
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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: 20140507 Termination date: 20211107 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |