CN201125231Y - Mobile biological diesel oil production facility - Google Patents
Mobile biological diesel oil production facility Download PDFInfo
- Publication number
- CN201125231Y CN201125231Y CNU2007200082863U CN200720008286U CN201125231Y CN 201125231 Y CN201125231 Y CN 201125231Y CN U2007200082863 U CNU2007200082863 U CN U2007200082863U CN 200720008286 U CN200720008286 U CN 200720008286U CN 201125231 Y CN201125231 Y CN 201125231Y
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- condenser
- connects
- production facility
- gas
- liquid separator
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- Expired - Fee Related
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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)
- Fats And Perfumes (AREA)
Abstract
The utility model provides a mobile type bio-diesel production equipment for preparing bio-diesel with recovery grease and methanol reaction. The production equipment uses a pipe type reacting furnace as main equipment, all equipment are installed in a frame convenient for convey equal to a container in size. The suit equipment provided by the utility model are concentrated in a frame equal to a container in size, and is convenient to convey and put into production. The mobile type bio-diesel production equipment reaches request of standardized equipment and standardized technique, has low cost and high return benefit.
Description
Technical field
The utility model belongs to the chemical industry equipment field, more specifically relates to a kind of to reclaim the mobile biodiesel production facility of grease and methyl alcohol prepared in reaction biofuel.
Background technology
With the grease is raw material, and the fatty acid methyl ester that obtains through methanol esterification can be used as diesel-fuel, the common name biofuel.Biofuel is in the fast development of a kind of reproducible green energy resource.American-European production biofuel is many to be raw material with alkali refining rapeseed oil and soybean oil, adopts the productions of base catalysis and methyl alcohol ester-interchange method.The main component of waste cooking oil and trench wet goods also is a lipid acid, can react synthesizing fatty acid methyl ester with methyl alcohol.But it is many to reclaim grease impurity, and the acid value height can not be used the base-catalyzed transesterification method.Use sulfuric acid, sulfonic acid etc. are as the acid esterification process of catalyzer, long reaction time, and inconvenient operation has spent acid to handle again, is not a kind of ideal method.Under the pressurization and the condition of heating, methyl esters and recovery grease can generate fatty acid methyl ester under the condition of catalyst-free, obtain meeting the biofuel of GB through underpressure distillation.
But there is complex manufacturing in present biofuel, technical problems such as equipment is huge, and waste cooking oil and trench wet goods refiltered oil fat resource are relatively disperseed and the human consumer of diesel oil also is a dispersive, and the transportation back and forth of raw material and product has also caused very big cost waste.
Goal of the invention
The utility model is at the problems referred to above, a kind of mobile biodiesel production facility is provided, this production unit is simple, can complete manufacturing and be installed in the framework of being convenient to carry of a freight container size, be convenient to move, can inject raw material after this device can being transported to suitable production site energising water flowing, through producing biofuel, avoided the transportation cost back and forth of raw material and product, production cost is low.
A kind of mobile biodiesel production facility of the present utility model, it is characterized in that: comprise the methanol tank 2 that is used to deposit the head tank 1 of glyceride stock and deposits methyl alcohol, described head tank 1 is connected with static mixer 5 by the pipeline that is provided with pump respectively with methanol tank 2, and described static mixer 5 connects and tubular react furnace 6 by pipeline; Described tubular react furnace 6 also is connected with flasher 7; Described flasher 7 is connected with raffinate basin 14, and described flasher 7 also connects first condenser 8 by the cut delivery conduit, and described first condenser 8 connects biofuel finished product basin 15 by first gas-liquid separator 11, water cooler 13; Described first gas-liquid separator 11 also is connected with second condenser 9, and described second condenser 9 connects work in-process basin 16 by second gas-liquid separator 12; Described second gas-liquid separator 12 also is connected with the 3rd condenser 10, and described the 3rd condenser 10 connects Methanol Recovery jar 17; The above equipment is installed in the framework of being convenient to carry of a freight container size.
Remarkable advantage of the present utility model is:
(1) equipment of the present utility model is installed in the framework of a freight container size, be convenient to the carrying, transport to production site after, connect water power and supporting storage tank, inject raw material and can produce, avoided the transportation cost back and forth of raw material and product, production cost is reduced, and productivity effect significantly improves.
(2) use the technical process of equipment of the present utility model simple, and adopt the DCS Controlling System to realize automatic red-tape operati, control is convenient.
(3) good product quality of use device fabrication of the present utility model, the diesel oil yield can reach about 90%.
Description of drawings
Fig. 1 is a mobile biodiesel production facility synoptic diagram of the present utility model, 1 head tank wherein, 2 methanol tanks, 3 pumps, 4 pumps, 5 static mixers, 6 tubular react furnaces, 7 flashers, 8 first condensers, 9 second condensers, 10 the 3rd condensers, 11 first gas-liquid separators, 12 second gas-liquid separators, 13 water coolers, 14 raffinate basins, 15 biofuel finished product basins, 16 work in-process basins, 17 Methanol Recovery jars, 18 spark arresters, 19 frameworks.
Embodiment
Carry out the production of biofuel according to mobile biodiesel production facility of the present utility model; Wherein also be provided with spark arrester 18 on the Methanol Recovery jar 17; Used pump is a triplex plunger pump.
Concrete technical process is as follows: glyceride stock is sent into static mixer 5 through pump 3 in the head tank 1, methyl alcohol in the methanol tank 2 is sent into static mixer 5 through pump 4, both mix back input tubular react furnace at static mixer 5 and react, described temperature of reaction is 300-600 ℃, and reaction pressure is 1-15Mpa; Reaction times is 1-20 minute; Cut after having reacted enters flasher 7 and isolate heavy cut to raffinate basin 14 under 360 ℃ of temperature; Uncooled gas enters first condenser 8 and is cooled to the part that 220 ℃ of condensations go out and is distilled product biofuel in flasher 7; Uncooled gas enters second condenser 9 and is cooled to 80 ℃ in first condenser 8, isolates aqueous middle distillate, and uncooled gas enters the 3rd condenser 10 and reclaims methyl alcohol in second condenser 9.
Uncooled gas discharges after incineration process in the 3rd condenser 10; Used glyceride stock is for reclaiming grease, comprises acidifying oil that waste cooking oil, sewer oil, refining raw food oil process obtain and in the deodorization distillate one or more.
The ratio of components of glyceride stock and methyl alcohol is that mol ratio is: 1: 0.5 to 1: 50.
Above-described technical process adopts the DCS Controlling System to realize automatic red-tape operati.
Claims (3)
1. mobile biodiesel production facility, it is characterized in that: comprise head tank (1) that is used to deposit glyceride stock and the methanol tank (2) of depositing methyl alcohol, described head tank (1) is connected with static mixer (5) by the pipeline that is provided with pump respectively with methanol tank (2), and described static mixer (5) connects and tubular react furnace (6) by pipeline; Described tubular react furnace (6) also is connected with flasher (7); Described flasher (7) is connected with raffinate basin (14), described flasher (7) also connects first condenser (8) by the cut delivery conduit, and described first condenser (8) connects biofuel finished product basin (15) by first gas-liquid separator (11), water cooler (13); Described first gas-liquid separator (11) also is connected with second condenser (9), and described second condenser (9) connects work in-process basins (16) by second gas-liquid separator (12); Described second gas-liquid separator (12) also is connected with the 3rd condenser (10), and described the 3rd condenser (10) connects Methanol Recovery jar (17); The above equipment is installed in the framework of being convenient to carry of a freight container size.
2. mobile biodiesel production facility according to claim 1 is characterized in that: also be provided with spark arrester (18) on the described Methanol Recovery jar (17).
3. mobile biodiesel production facility according to claim 1 is characterized in that: described pump is a triplex plunger pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200082863U CN201125231Y (en) | 2007-09-21 | 2007-09-21 | Mobile biological diesel oil production facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200082863U CN201125231Y (en) | 2007-09-21 | 2007-09-21 | Mobile biological diesel oil production facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201125231Y true CN201125231Y (en) | 2008-10-01 |
Family
ID=39998648
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007200082863U Expired - Fee Related CN201125231Y (en) | 2007-09-21 | 2007-09-21 | Mobile biological diesel oil production facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201125231Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010085864A1 (en) * | 2009-01-27 | 2010-08-05 | Biominas Indústria De Derivados Oleaginosos Ltda | Self-sustainable mobile biodiesel production plant and method |
| CN103117407A (en) * | 2013-02-04 | 2013-05-22 | 吉首市汇锋矿业有限责任公司 | Mobile vanadium electrolyte preparation device and vanadium electrolyte preparation method |
| CN103897803A (en) * | 2014-03-13 | 2014-07-02 | 深圳市朗坤环保有限公司 | Process and system for purifying biodiesel |
| GB2509938A (en) * | 2013-01-17 | 2014-07-23 | Robert Graham Beardwell | Biodiesel processor |
| CN106318646A (en) * | 2016-09-22 | 2017-01-11 | 常州工程职业技术学院 | Device and method for continuous methyl esterification of high-acid value illegal cooking oil through pressurized catalysis |
-
2007
- 2007-09-21 CN CNU2007200082863U patent/CN201125231Y/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010085864A1 (en) * | 2009-01-27 | 2010-08-05 | Biominas Indústria De Derivados Oleaginosos Ltda | Self-sustainable mobile biodiesel production plant and method |
| US8398942B2 (en) | 2009-01-27 | 2013-03-19 | Biominas Industria de Derivados Oleaginosos Ltda. | Self-sustainable mobile biodiesel production plant and method |
| GB2509938A (en) * | 2013-01-17 | 2014-07-23 | Robert Graham Beardwell | Biodiesel processor |
| GB2509938B (en) * | 2013-01-17 | 2014-12-03 | Robert Graham Beardwell | Biodiesel Processor |
| CN103117407A (en) * | 2013-02-04 | 2013-05-22 | 吉首市汇锋矿业有限责任公司 | Mobile vanadium electrolyte preparation device and vanadium electrolyte preparation method |
| CN103117407B (en) * | 2013-02-04 | 2015-03-11 | 湖南汇锋高新能源有限公司 | Mobile vanadium electrolyte preparation device and vanadium electrolyte preparation method |
| CN103897803A (en) * | 2014-03-13 | 2014-07-02 | 深圳市朗坤环保有限公司 | Process and system for purifying biodiesel |
| CN103897803B (en) * | 2014-03-13 | 2015-09-30 | 深圳市朗坤环保有限公司 | Biofuel purifying technique and system |
| CN106318646A (en) * | 2016-09-22 | 2017-01-11 | 常州工程职业技术学院 | Device and method for continuous methyl esterification of high-acid value illegal cooking oil through pressurized catalysis |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20081001 Termination date: 20130921 |