CN204550502U - A kind of biofuel is automatic glycerin soap separator continuously - Google Patents
A kind of biofuel is automatic glycerin soap separator continuously Download PDFInfo
- Publication number
- CN204550502U CN204550502U CN201520077174.8U CN201520077174U CN204550502U CN 204550502 U CN204550502 U CN 204550502U CN 201520077174 U CN201520077174 U CN 201520077174U CN 204550502 U CN204550502 U CN 204550502U
- Authority
- CN
- China
- Prior art keywords
- cylindrical shell
- methyl esters
- glycerine
- glycerin soap
- soap
- 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
Links
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 title claims abstract description 86
- 235000011187 glycerol Nutrition 0.000 title claims abstract description 43
- 239000000344 soap Substances 0.000 title claims abstract description 29
- 239000002551 biofuel Substances 0.000 title claims abstract description 10
- 150000004702 methyl esters Chemical class 0.000 claims abstract description 23
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 230000009257 reactivity Effects 0.000 abstract description 3
- 239000000463 material Substances 0.000 description 4
- 238000004062 sedimentation Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 235000019387 fatty acid methyl ester Nutrition 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000005809 transesterification reaction Methods 0.000 description 1
Classifications
-
- 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
Landscapes
- Detergent Compositions (AREA)
Abstract
The utility model discloses a kind of biofuel automatic glycerin soap separator continuously, comprise cylindrical shell and leg; Described cylindrical shell is laterally fixed on leg, and one end of cylindrical shell is provided with opening for feed, and the upper and lower of the other end is respectively equipped with the outlet of thick methyl esters and glycerin soap collection bucket, and the bottom of glycerin soap collection bucket is provided with and goes out glycerine mouth continuously; The baffle plate that polylith is vertically arranged is provided with in the inner chamber of described cylindrical shell.The utility model achieves serialization and is separated, decrease because of manually-operated uncontrollability, methyl esters in the glycerine separated like this is few, the content of raw glycerine can reach about 80%, and the glycerine in methyl esters can be controlled in 0.05%, soap content can be controlled in 0.1%, be convenient to tower rectifying on thick methyl esters, than the thick methyl esters rectification yield height 2-3% of traditional equal reactivity, and achieve production serialization.
Description
Technical field
The utility model relates to a kind of biofuel automatic glycerin soap separator continuously.
Background technology
Glycerine, soap, fatty acid methyl ester, a small amount of neutral grease, catalyzer is had in material after transesterification reaction; it is crucial for how being separated, and mostly major part biofuel enterprise of China is natural subsidence, and the time, long-acting rate was low; can not continuous prodution, do not meet the requirement of large-scale production.Because a tank one puts glycerine, manual operation reason is more, makes in glycerine many containing methyl esters, or the ratio containing glycerine, soap in methyl esters is many.
Utility model content
The purpose of this utility model is to provide a kind of biofuel automatic glycerin soap separator continuously, reduces because of manually-operated uncontrollability, can separate the glycerin soap that methyl esters is few, raw glycerine content is high, and the methyl esters that the ratio containing glycerine and soap is few.
The technical scheme realizing the utility model object is: a kind of biofuel is automatic glycerin soap separator continuously, comprises cylindrical shell and leg; Described cylindrical shell is laterally fixed on leg, and one end of cylindrical shell is provided with opening for feed, and the upper and lower of the other end is respectively equipped with the outlet of thick methyl esters and glycerin soap collection bucket, and the bottom of glycerin soap collection bucket is provided with and goes out glycerine mouth continuously; The baffle plate that polylith is vertically arranged is provided with in the inner chamber of described cylindrical shell.
Described inner barrel is arranged on the inner cavity top of cylindrical shell near first piece of baffle plate of opening for feed, and other baffle plate is arranged on inner cavity top or the middle part of cylindrical shell.
Have employed technique scheme, the utility model has following beneficial effect: (1) the utility model achieves serialization and is separated, decrease because of manually-operated uncontrollability, methyl esters in the glycerine separated like this is few, the content of raw glycerine can reach about 80%, and the glycerine in methyl esters can be controlled in 0.05%, soap content can be controlled in 0.1%, be convenient to tower rectifying on thick methyl esters, than the thick methyl esters rectification yield height 2-3% of traditional equal reactivity, and achieve production serialization.
(2) inner barrel of the present utility model is arranged on the inner cavity top of cylindrical shell near first piece of baffle plate of opening for feed, other baffle plate is arranged on inner cavity top or the middle part of cylindrical shell, this structure can make the sedimentation downwards better of glycerine and soap, improves separation efficiency.
Accompanying drawing explanation
In order to make content of the present utility model more easily be clearly understood, below according to specific embodiment also by reference to the accompanying drawings, the utility model is described in further detail, wherein
Fig. 1 is structural representation of the present utility model.
Label in accompanying drawing is:
Cylindrical shell 1, opening for feed 11, thick methyl esters outlet 12, glycerin soap collection bucket 13, go out glycerine mouth 14, baffle plate 15, leg 2 continuously.
Embodiment
(embodiment 1)
See Fig. 1, the biofuel automatic glycerin soap separator continuously of the present embodiment, comprises cylindrical shell 1 and leg 2.
Cylindrical shell 1 is laterally fixed on leg 2, and one end of cylindrical shell 1 is provided with opening for feed 11, and the upper and lower of the other end is respectively equipped with thick methyl esters outlet 12 and glycerin soap collection bucket 13, and the bottom of glycerin soap collection bucket 13 is provided with and goes out glycerine mouth 14 continuously.The baffle plate 15 that polylith is vertically arranged is provided with in the inner chamber of cylindrical shell 1.The inner first piece of baffle plate 15 near opening for feed 11 of cylindrical shell 1 is arranged on the inner cavity top of cylindrical shell 1, and other baffle plate 15 is arranged on inner cavity top or the middle part of cylindrical shell 1.
Mixture enters cylindrical shell 1 by opening for feed 11 continuously, is forced the flow direction of material by baffle plate 15, makes glycerine and the downward sedimentation of soap, is ensured the settling time of material by the volume of cylindrical shell 1, and the material that sedimentation is good flows out continuously from thick methyl esters outlet 12.Glycerine and soap are discharged continuously from glycerin soap collection bucket 13, achieve serialization to be separated, decrease because of manually-operated uncontrollability, methyl esters in the glycerine separated like this is few, the content of raw glycerine can reach about 80%, and the glycerine in methyl esters can be controlled in 0.05%, soap content can be controlled in 0.1%, be convenient to tower rectifying on thick methyl esters, than the thick methyl esters rectification yield height 2-3% of traditional equal reactivity, and achieve production serialization.
Above-described specific embodiment; the purpose of this utility model, technical scheme and beneficial effect are further described; be understood that; the foregoing is only specific embodiment of the utility model; be not limited to the utility model; all within spirit of the present utility model and principle, any amendment made, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (2)
1. a biofuel automatic glycerin soap separator continuously, is characterized in that: comprise cylindrical shell (1) and leg (2); Described cylindrical shell (1) is laterally fixed on leg (2), one end of cylindrical shell (1) is provided with opening for feed (11), the upper and lower of the other end is respectively equipped with the outlet of thick methyl esters (12) and glycerin soap collection bucket (13), and the bottom of glycerin soap collection bucket (13) is provided with and goes out glycerine mouth (14) continuously; The baffle plate (15) that polylith is vertically arranged is provided with in the inner chamber of described cylindrical shell (1).
2. a kind of biofuel according to claim 1 automatic glycerin soap separator continuously, it is characterized in that: the inner first piece of baffle plate (15) near opening for feed (11) of described cylindrical shell (1) is arranged on the inner cavity top of cylindrical shell (1), and other baffle plate (15) is arranged on inner cavity top or the middle part of cylindrical shell (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520077174.8U CN204550502U (en) | 2015-02-03 | 2015-02-03 | A kind of biofuel is automatic glycerin soap separator continuously |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520077174.8U CN204550502U (en) | 2015-02-03 | 2015-02-03 | A kind of biofuel is automatic glycerin soap separator continuously |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204550502U true CN204550502U (en) | 2015-08-12 |
Family
ID=53825638
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520077174.8U Expired - Fee Related CN204550502U (en) | 2015-02-03 | 2015-02-03 | A kind of biofuel is automatic glycerin soap separator continuously |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204550502U (en) |
-
2015
- 2015-02-03 CN CN201520077174.8U patent/CN204550502U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201962220U (en) | Solid continuous distillation device | |
| CN204550502U (en) | A kind of biofuel is automatic glycerin soap separator continuously | |
| CN201701770U (en) | Tower internal reflux distributor | |
| CN203715626U (en) | System for fermenting biogas by utilizing kitchen waste oil | |
| CN212357409U (en) | Solar energy hydrolysis hydrogen production device | |
| CN102634446A (en) | High-concentration position pressure type self-slagging methane generating pond | |
| CN202951286U (en) | Glycerin water purification tank | |
| CN103497842B (en) | The first and second alcohol are utilized to prepare the novel method of biofuel as ester exchange agent | |
| CN105001983A (en) | Method for reducing acid values of waste oils and fats by extraction esterification | |
| CN101250082A (en) | Preparation method of alpha-methylnaphthalene | |
| CN201908081U (en) | A distiller for yellow water produced by wine brewing | |
| CN205990443U (en) | The equipment for separating liquid from solid extracting for noble metal | |
| CN106281483B (en) | A method of preparing biodiesel by raw material of algae | |
| CN104120039A (en) | Method for preparing fatty acid methyl ester through multi-stage ester exchange | |
| CN204981828U (en) | Batch production apparatus for biodiesel | |
| CN201330242Y (en) | Production equipment for refining biodiesel | |
| CN202610226U (en) | High-concentration level-pressure type automatic-deslagging biogas generation tank | |
| CN103194255A (en) | Method for producing clean fuels by catalyzing and cracking animal and vegetable oil | |
| CN202909491U (en) | Continuous separation device for producing biodiesel | |
| CN202777873U (en) | Novel three-stage rectifying tower | |
| CN209188198U (en) | Thick methyl esters Quick Separation System is exclusively used in production of biodiesel | |
| CN202175450U (en) | Discharging station | |
| CN201719924U (en) | Simple tail gas separation device | |
| CN201815147U (en) | Vertical type oil-water separator | |
| CN201286992Y (en) | Purification and filtration device of extract liquid |
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: 20150812 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |