CN200967808Y - Environment-friendly type esterification device for producing biological diesel - Google Patents
Environment-friendly type esterification device for producing biological diesel Download PDFInfo
- Publication number
- CN200967808Y CN200967808Y CNU2006201491302U CN200620149130U CN200967808Y CN 200967808 Y CN200967808 Y CN 200967808Y CN U2006201491302 U CNU2006201491302 U CN U2006201491302U CN 200620149130 U CN200620149130 U CN 200620149130U CN 200967808 Y CN200967808 Y CN 200967808Y
- Authority
- CN
- China
- Prior art keywords
- discharge port
- container
- mainly
- esterification
- environment
- 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
Images
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
- 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
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Liquid Carbonaceous Fuels (AREA)
Abstract
The utility model relates to an environmental protective estrification plant to produce biologic diesel oil, and primarily comprises an esterification (transesterification) reactor and a liquid misphasing segregator. The esterification reactor primarily consists of a container, a feed inlet, a discharge port, a motor stirrer, a heating device and a catalyzer feed port. The liquid misphasing segregator primarily consists of a container, a feed inlet, a discharge port, a methyl ester outlet and a glycerol discharge port. The utility model is characterized in that guide plates are longitudinally fixed on inner wall of the container; the bottom of the container is of conical shape; a filter is provided in the middle of the conical bottom; a compressed air inlet is connected to the discharge port; a proportioner is provided between the catalyzer feed port and the container; the heating device consists of a serpentuator arranged inside the container, a vapor inlet and a vapor outlet. A methanol reflux device is provided on top of the container. The utility model is applicable for production of biologic diesel oil, and is characterized in proper structure, short flow path, high percent conversion, energy conservation, environmental protection and high diesel oil quality.
Description
Technical field
The utility model belongs to a kind of biodiesel oil producing apparatus, and concrete is a kind ofly makes raw material with various animals and plants greases, carries out esterification with an acidic catalyst, and producing fatty acid methyl ester is the device of biofuel.
Background technology
Because a variety of causes, the fuel oil of various countries problem order benefit in short supply is serious, and the pollution of petroleum products is also more and more paid attention to by people, and therefore, greatly developing biofuel and various bio-fuel-oil is a very important task.At present, the technology and equipments about the production biofuel have appearred much, they all in various degree solution the basic fundamental problem of production biofuel.But come with some shortcomings mostly: must use stainless steel equipment, cost height; Use strong acid or alkali catalyst that environment is caused heavier pollution; Esterification is abundant inadequately, and transformation efficiency is not high; Adaptability to raw material is not strong; Production process control out of true, the quality of product is high inadequately.Therefore, it is more reasonable to need to propose a kind of structure, and equipment cost is low, and is free from environmental pollution, the technology and equipment that production efficiency and quality are high.
The utility model content
The purpose of this utility model is at the problems referred to above, proposes a kind of esterification device of environment-friendly type production biofuel, and this apparatus structure has bigger improvement, can make with plain carbon stool, use the weak acid solid catalyst, environment is not polluted, have and produce preferably and social effect.
The purpose of this utility model is achieved through the following technical solutions: a kind of esterification device of environment-friendly type production biofuel, comprise mainly and give esterifier and liquid divides phase separator that the described esterifier that gives mainly adds inlet by tank body, opening for feed, discharge port, electric mixer, heating unit, catalyst and forms; Described liquid divides phase separator mainly to be made up of tank body, opening for feed, discharge port, methyl esters outlet, glycerol outlet port; It is characterized in that: the described esterifier that gives also is provided with the flow deflector that is vertically fixed in inner tank wall, described tank base is taper, be provided with strainer in the middle of this conical lower portion, be connected to a compressed air inlet at described discharge port, catalyzer add the inlet and tank body between be provided with a batchmeter, described heating unit is formed by being located at jar intravital serpentine tube and water vapor import and steam outlet, with water vapor or hot water heating; Top at tank body also is provided with the methanol eddy device, and this device mainly is made up of distillation column and condensate cooler; The discharge port that will give esterifier by pipe connecting divides the opening for feed of phase separator to be connected with liquid.
The additional project of further improving and implementing of the present utility model is:
Described liquid divides phase separator also to be provided with every stream plate washer, light phase liquidometer and heavy phase liquidometer.
Described glycerol outlet port place is provided with an automatic escaper of glycerine, and this escaper mainly is made up of discharging glycerine optic cup, glycerine separator tube and switch.
The utility model is provided with vertical thrust-augmenting nozzle and pressurized air and adds the structure of strong mixing from the bottom injection, so can adapt to various raw materials owing to adopted steam or the serpentine tube structure of hot water heating, and stir, sufficient reacting, esterification turnover ratio height, good product quality; Adopted the catalyzer dosing device, the consumption of control catalyst more accurately, the methanol eddy device can better reclaim methyl alcohol; The bottom of taper and filtration unit can be controlled better and enter the quality that liquid divides the mixed solution of phase separator; Divide at liquid that be provided with in the phase separator can be so that the new mixed solution that injects can not mix with isolating glycerine and methyl esters every the stream plate washer, assurance methyl esters phase-splitting separating effect is better; Being provided with the glycerine automatic segregator can separate glycerine purelyr.Therefore, the utlity model has following advantage: adapt to various glyceride stocks; Use the plain carbon stool low cost of manufacture; Can use little acid catalyst free from environmental pollution; Esterification is abundant, and glycerine separates pure with methyl esters, and flow process is short, the transformation efficiency height, and the output high quality of production biofuel is good.
Description of drawings
Below in conjunction with drawings and Examples the utility model is described further:
Fig. 1 is a main TV structure synoptic diagram of the present utility model;
Fig. 2 is the vertical view that liquid of the present utility model divides phase separator.
Embodiment
Embodiment: referring to accompanying drawing, a kind of esterification device of environment-friendly type production biofuel, comprise mainly and give esterifier and liquid divides phase separator that the described esterifier that gives mainly adds inlet 3 by tank body 7, opening for feed 6, discharge port 13, electric mixer 10, heating unit, catalyst and forms; Described liquid divides phase separator mainly to be made up of tank body 2, opening for feed 2.1, discharge port 2.2, methyl esters outlet 2.6, glycerol outlet port 3.3; The described esterifier that gives also is provided with the flow deflector 9 that is vertically fixed in inner tank wall, described tank base is taper, is provided with strainer 11 in the middle of this conical lower portion, is connected to a compressed air inlet 12 at described discharge port, catalyzer add the inlet and tank body between be provided with a batchmeter 16, this batchmeter is made up of two switches, closes following switch, opens top switch, after the catalyzer that enters is an amount of, close top switch again, open following switch, make quantitative catalyzer inject tank body; Described heating unit is formed by being located at jar intravital serpentine tube 15 and water vapor import 8 and steam outlet 14, with water vapor or hot water heating; Top at tank body also is provided with the methanol eddy device, and this device mainly is made up of distillation column 5 and condensate cooler 4; The discharge port that will give esterifier by pipe connecting 1 divides the opening for feed 2.1 of phase separator to be connected with liquid.Described liquid divides phase separator also to be provided with every stream plate washer 2.5, light phase liquidometer 2.3 and heavy phase liquidometer 2.4, and light phase liquidometer is in order to observe the methyl esters separation case, and the heavy phase liquidometer is in order to observe the glycerine separation case.Described glycerol outlet port place is provided with an automatic escaper of glycerine, and this escaper mainly is made up of discharging glycerine optic cup 3.1, glycerine separator tube 3.2 and switch.The utility model plain carbon stool manufacturing also is provided with in addition in order to accessories such as the population safeguarded and fixed supports.
Detect through relevant department, product quality of the present utility model, environment protecting all meets or exceeds relevant Standard has obvious advantage.
Claims (3)
1, a kind of esterification device of environment-friendly type production biofuel, comprise that mainly esterification (transesterify) reactor and liquid divide phase separator, described esterifier is mainly added inlet (3) and is formed by tank body (7), opening for feed (6), discharge port (13), electric mixer (10), heating unit, catalyst; Described liquid divides phase separator mainly to be made up of tank body (2), opening for feed (2.1), discharge port (2.2), methyl esters outlet (2.6), glycerol outlet port (3.3); It is characterized in that: the described esterifier that gives also is provided with the flow deflector (9) that is vertically fixed in inner tank wall, described tank base is taper, be provided with strainer (11) in the middle of this conical lower portion, be connected to a compressed air inlet (12) at described discharge port, catalyzer add the inlet and tank body between be provided with a batchmeter (16), described heating unit is formed by being located at jar intravital serpentine tube (15) and water vapor import (8) and steam outlet (14), with water vapor or hot water heating; Top at tank body also is provided with the methanol eddy device, and this device mainly is made up of distillation column (5) and condensate cooler (4); The discharge port that will give esterifier by pipe connecting (1) divides the opening for feed (2.1) of phase separator to be connected with liquid.
2, the esterification device of environment-friendly type production biofuel according to claim 1 is characterized in that: described liquid divides phase separator also to be provided with every stream plate washer (2.5) light phase liquidometer (2.3) and heavy phase liquidometer (2.4).
3, the esterification device of environment-friendly type production biofuel according to claim 1, it is characterized in that: described glycerol outlet port place is provided with an automatic escaper of glycerine, and this escaper mainly is made up of discharging glycerine optic cup (3.1), glycerine separator tube (3.2) and switch.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006201491302U CN200967808Y (en) | 2006-10-26 | 2006-10-26 | Environment-friendly type esterification device for producing biological diesel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006201491302U CN200967808Y (en) | 2006-10-26 | 2006-10-26 | Environment-friendly type esterification device for producing biological diesel |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200967808Y true CN200967808Y (en) | 2007-10-31 |
Family
ID=38967377
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2006201491302U Expired - Fee Related CN200967808Y (en) | 2006-10-26 | 2006-10-26 | Environment-friendly type esterification device for producing biological diesel |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN200967808Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101805673A (en) * | 2010-04-01 | 2010-08-18 | 江苏大学 | Airlifting biodiesel ester exchange reactor |
| US20100261235A1 (en) * | 2007-12-14 | 2010-10-14 | Kansai Chemical Engineering Co., Ltd. | Continuous production of biodiesel fuel by enzymatic method |
| CN102559396A (en) * | 2012-01-18 | 2012-07-11 | 浙江工业大学 | Biodiesel esterification ester exchange reaction device |
| CN103160381A (en) * | 2013-04-09 | 2013-06-19 | 成都恒润高新科技有限公司 | Special equipment for preparing biodiesel |
| CN107051270A (en) * | 2016-12-30 | 2017-08-18 | 广西利升石业有限公司 | A kind of high efficiency resin heats bucket |
-
2006
- 2006-10-26 CN CNU2006201491302U patent/CN200967808Y/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100261235A1 (en) * | 2007-12-14 | 2010-10-14 | Kansai Chemical Engineering Co., Ltd. | Continuous production of biodiesel fuel by enzymatic method |
| US9879291B2 (en) | 2007-12-14 | 2018-01-30 | Kansai Chemical Engineering Co., Ltd. | Continuous production of biodiesel fuel by enzymatic method |
| CN101805673A (en) * | 2010-04-01 | 2010-08-18 | 江苏大学 | Airlifting biodiesel ester exchange reactor |
| CN102559396A (en) * | 2012-01-18 | 2012-07-11 | 浙江工业大学 | Biodiesel esterification ester exchange reaction device |
| CN102559396B (en) * | 2012-01-18 | 2013-10-30 | 浙江工业大学 | Biodiesel esterification ester exchange reaction device |
| CN103160381A (en) * | 2013-04-09 | 2013-06-19 | 成都恒润高新科技有限公司 | Special equipment for preparing biodiesel |
| CN103160381B (en) * | 2013-04-09 | 2015-07-08 | 成都恒润高新科技有限公司 | Special equipment for preparing biodiesel |
| CN107051270A (en) * | 2016-12-30 | 2017-08-18 | 广西利升石业有限公司 | A kind of high efficiency resin heats bucket |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203474762U (en) | Continuous esterification reactor and device | |
| CN200967808Y (en) | Environment-friendly type esterification device for producing biological diesel | |
| CN102311883B (en) | Method for preparing high-purity biodiesel | |
| CN100434164C (en) | Catalyst system and biological diesel oil producing process with the catalyst system | |
| CN105623861B (en) | A kind of glycerine esterification reaction unit | |
| CN1687312A (en) | Method for producing biologic diesel oil through waterpower cavitation | |
| CN200951999Y (en) | Apparatus for producing biological diesel oil | |
| CN203212544U (en) | Flash dealcoholizing separating device of coarse methyl ester | |
| CN103242966A (en) | Technology process for producing biodiesel and key preparation device | |
| CN101117587B (en) | Mobile biodiesel production facility and its process flow | |
| CN202063896U (en) | Solid acid biodiesel production equipment of mobile multi-group serial fixed bed | |
| CN201125231Y (en) | Mobile biological diesel oil production facility | |
| CN201330241Y (en) | Device for producing refined biodiesel with high acid value oil | |
| CN201272776Y (en) | Apparatus for continuous preparation of biodiesel by neutral grease | |
| CN2883376Y (en) | Biological diesel continuous prodn. plant | |
| CN103060097A (en) | Continuous production line for producing biodiesel under catalysis of solid catalyst | |
| CN201482341U (en) | Furfural gas filter device and hydrolytic kettle provided therewith | |
| CN204848822U (en) | Serialization bio diesel oil device | |
| CN204455053U (en) | A kind of modified version biodiesel esterification device | |
| CN101486923A (en) | Environment friendly process for biodiesel | |
| CN216513753U (en) | Esterification reaction device for preparing biodiesel from waste animal and vegetable oil | |
| KR102172951B1 (en) | Biodiesel continuous production system and method using biodiesel manufacturing reactor and electric conductivity | |
| CN101067090B (en) | Solid catalysis for preparing biodiesel oil | |
| CN101113351A (en) | Solid catalytic production method of biodiesel | |
| CN201330242Y (en) | Production equipment for refining biodiesel |
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: 20071031 Termination date: 20151026 |
|
| EXPY | Termination of patent right or utility model |