CN201068443Y - Glycerol separation apparatus for biodiesel production - Google Patents
Glycerol separation apparatus for biodiesel production Download PDFInfo
- Publication number
- CN201068443Y CN201068443Y CNU2007200068601U CN200720006860U CN201068443Y CN 201068443 Y CN201068443 Y CN 201068443Y CN U2007200068601 U CNU2007200068601 U CN U2007200068601U CN 200720006860 U CN200720006860 U CN 200720006860U CN 201068443 Y CN201068443 Y CN 201068443Y
- Authority
- CN
- China
- Prior art keywords
- glycerin
- glycerine
- biological diesel
- reaction
- biofuel
- 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 - Lifetime
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
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- Liquid Carbonaceous Fuels (AREA)
Abstract
The utility model discloses a glycerin separating device of biological diesel in the production process. The device is provided with a glycerin discharging pipe 2 at the bottom part of a reaction vessel 1 of the biological diesel, the glycerin discharging pipe 2 is connected with a glycerin separating tank 4 through a connecting valve 3, and a return pipe 5 of the biological diesel is arranged between the glycerin separating tank 4 and the reaction vessel 1 of the biological diesel. According to the actual conditions during the reaction process, the glycerin generated during the reaction process is discharged into the glycerin separating tank 4 with the fixed time and the fixed quantity or continuously, the balanced state of the chemical reaction is broken, so as to prompt the reversible reaction to move towards the direction where the biological diesel and the glycerin are generated, therefore, the conversion rate of the biological diesel can be improved to over 98 percent from 92 percent, the triglyceride content in the biological diesel can be reduced, the product color can be decreased, and the product quality can be improved.
Description
One, technical field
The utility model relates to the production equipment of organic Chemicals biofuel (fatty acid methyl ester), is specifically related to the glycerine tripping device in the production of biodiesel process.
Two, background technology
In the existing production of biodiesel, animal-plant oil or the animal-plant oil that contains small-amount free lipid acid are under catalyzer, excessive methanol environment, reflux, reaction generates biofuel and glycerine, and this chemical reaction belongs to reversible reaction, when the transformation efficiency of animal-plant oil biodiesel synthesis reaches 92% left and right sides, reversible reaction reaches equilibrium state, finish reaction, slough methyl alcohol, glycerine is separated from biofuel.Owing to do not adopt glycerine separation facilities separation of glycerin in the biofuel chemical reaction process, reaction is difficult to go on again when reaction is in reversible equilibrium state, influence the biofuel recovery rate, and content of triglyceride height in the biofuel, the biofuel quality influenced.
Three, summary of the invention
The purpose of this utility model provides the glycerine tripping device in the production of biodiesel process of a kind of biofuel transformation efficiency height, good product quality.
For realizing above purpose, glycerine tripping device in the utility model production of biodiesel process is established the glycerine discharge nozzle in biofuel reactor bottom, connect the glycerine separating tank by connecting valve, between glycerine separating tank biofuel reactor, also be provided with and the biofuel return line.
When the reversible reaction that is converted into biofuel and glycerine when grease and methyl alcohol under the effect at catalyzer reaches equilibrium state, from reaction system, isolate the glycerine of generation by the glycerine tripping device, break the equilibrium state of chemical reaction, impel reversible reaction to continue to carry out to the direction that generates biofuel and glycerine, the biofuel transformation efficiency can be brought up to more than 98% from 92%, reduce content of triglyceride in the biofuel, reduce product color, improve the quality of products thereby improve purity.
Four, description of drawings
Fig. 1 is the glycerine tripping device synoptic diagram in the utility model production of biodiesel process.
Five, specific embodiment
Below in conjunction with Fig. 1 and embodiment the utility model is described in further detail.
Glycerine tripping device in the utility model production of biodiesel process shown in Figure 1 is established glycerine discharge nozzle 2 in biofuel reactor 1 bottom, connect glycerine separating tank 4 by connecting valve 3, between glycerine separating tank 4 biofuel reactors 1, also be provided with and biofuel return line 5, because glycerine proportion larger part is beneficial to automatic separation in the reactor bottom, according to the reaction process particular case, at regular time and quantity or continuously the glycerine that generates in the reaction process is drained into glycerine separating tank 4 by valve 3, on a small quantity the biofuel that drains into glycerine separating tank 4 with glycerine is back to reactor 1 because of proportion is less by return line 5, realizes that glycerine separates automatically in the biofuel chemical reaction process.
Claims (1)
1. the glycerine tripping device in the production of biodiesel process, it is characterized in that: establish glycerine discharge nozzle (2) in biofuel reactor (1) bottom, connect glycerine separating tank (4) by connecting valve (3), between glycerine separating tank (4) biofuel reactor (1), also be provided with and biofuel return line (5).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNU2007200068601U CN201068443Y (en) | 2007-04-19 | 2007-04-19 | Glycerol separation apparatus for biodiesel production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNU2007200068601U CN201068443Y (en) | 2007-04-19 | 2007-04-19 | Glycerol separation apparatus for biodiesel production |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201068443Y true CN201068443Y (en) | 2008-06-04 |
Family
ID=39489819
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNU2007200068601U Expired - Lifetime CN201068443Y (en) | 2007-04-19 | 2007-04-19 | Glycerol separation apparatus for biodiesel production |
Country Status (1)
Country | Link |
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CN (1) | CN201068443Y (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103013673A (en) * | 2012-12-10 | 2013-04-03 | 中国科学院广州能源研究所 | Continuous separation method and device for producing glycerin from biodiesel |
CN109621858A (en) * | 2018-12-25 | 2019-04-16 | 福州大学 | A method of using catalyst wall loadization microreactor and the tiny segregator with interfacial property difference synthesizes and separation biodiesel |
-
2007
- 2007-04-19 CN CNU2007200068601U patent/CN201068443Y/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103013673A (en) * | 2012-12-10 | 2013-04-03 | 中国科学院广州能源研究所 | Continuous separation method and device for producing glycerin from biodiesel |
CN109621858A (en) * | 2018-12-25 | 2019-04-16 | 福州大学 | A method of using catalyst wall loadization microreactor and the tiny segregator with interfacial property difference synthesizes and separation biodiesel |
CN109621858B (en) * | 2018-12-25 | 2021-01-29 | 福州大学 | Method for synthesizing and separating biodiesel by utilizing catalyst wall-supported microreactor and micro-separator with interface property difference |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C56 | Change in the name or address of the patentee |
Owner name: LONGYAN ZHUOYUE NEW ENERGY CO., LTD. Free format text: FORMER NAME: LONGYAN ZHUOYUE NEW ENERGY DEVELOPMENT CO., LTD. |
|
CP01 | Change in the name or title of a patent holder |
Address after: 364001 Tieshan Development Zone, Xinluo District, Fujian, Longyan Patentee after: Longyan Zhuoyue New Energy Co., Ltd. Address before: 364001 Tieshan Development Zone, Xinluo District, Fujian, Longyan Patentee before: Longyan Zhuoyue New Energy Development Co., Ltd. |
|
CX01 | Expiry of patent term |
Granted publication date: 20080604 |
|
CX01 | Expiry of patent term |