CN101134903A - Mobile biodiesel producing base station - Google Patents
Mobile biodiesel producing base station Download PDFInfo
- Publication number
- CN101134903A CN101134903A CNA2006101122321A CN200610112232A CN101134903A CN 101134903 A CN101134903 A CN 101134903A CN A2006101122321 A CNA2006101122321 A CN A2006101122321A CN 200610112232 A CN200610112232 A CN 200610112232A CN 101134903 A CN101134903 A CN 101134903A
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- China
- Prior art keywords
- alcohols
- jar
- base station
- hybrid reaction
- catalyst
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- 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.)
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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
Abstract
The mobile biodiesel oil producing base station consists of a moving unit, one oil discharging unit, an oil storing tank, a evaporating unit, an animal and vegetable oil storing tank, a catalyst preparing tank, a alcohol storing tank, a mixing reactor, a heater, a setting tank, a centrifuging unit and other units. It features the catalyst prepared with sodium sulfate and strong alkali inside the catalyst preparing tank, the mixing of animal and vegetable oil, composite catalyst and alcohols in certain weight proportion inside the mixing reactor at certain temperature, the separation among heavy liquid, fatting soap, catalyst and light liquid inside the centrifuging unit, the separation of light liquid in the evaporating unit into alcohols and alcohol ester, and the movable platform for all the units to be installed on and connected through a pipeline with valves and pumps.
Description
Technical field
A kind of mobile biodiesel producing base station belongs to fuel oil supply technical field.
Technical background
Along with global power supply anxiety, each state all in the biotechnology of actively researching and developing alternative oil, has also proposed many animal-plant oil that utilize and has been main raw material, the preparation method of bio-diesel oil.But these methods all be basically with animal-plant oil in certain temperature, pressure condition under the effect of catalyzer, carry out transesterification reaction with low-carbon alcohol such as methyl alcohol or ethanol, generating fatty acid methyl ester is alcohol ester, just so-called biofuel.The recovery rate of technology is very high, and finished product also can reach the relevant criterion of diesel oil.But the prior art defective is, when adopting soda acid to make catalyzer, the religion of soda acid consumption is big, and the reaction times is longer, and environmental pollution is very serious; Adopt enzyme to make the method for catalyzer, then enzyme dosage is big, costs an arm and a leg, and the reaction times is longer, and the cost religion of resultant is high.The technology relative complex that both are required needs large-scale conversion unit, can only build up relatively large factory.And need the mobile can be with biofuel as the equipment of the energy concerning those, just very inconvenient, for example army is in State of War, the supply of petroleum-based energy is blocked, when surrounding environment has collectable animal-plant oil resource again, but do not have movably, fast animal-plant oil to be converted into the making equipment of biofuel, equipment does not have power, causes fighting capacity to descend.
Summary of the invention
The purpose of this invention is to provide a kind of mobile biodiesel producing base station scheme, and the preparation method of corresponding biofuel.
Technical scheme of the present invention is achieved like this: 1, collect vegetable and animals oils, and it is stand-by to be stored in storage tank: this two classes oil, available manufactured processed oil, also can be with the processed finished products depleted waste product oil in when oil, or even the waste oil of used or corrupt high acid value; 2, prepare weakly alkaline composite catalyst, at first with organic sulfite and highly basic (NaOH) according to the kind of collecting oil, the ratio by weight 1: 3～12 feeds intake, and in the retort of preparation catalyzer, through stirring thorough mixing, obtains the weakly alkaline composite catalyst; 3, with the grease of collecting, organic appearance agent (alcohols), weakly alkaline composite catalyst, by weight percentage: 100: 1O～50: 0.5～5 feed intake in airtight batch mixing retort, control heating at a certain temperature, through stirring, after the backflow, place in the airtight retort, under 50～100 ℃ temperature of reaction, after fully stirring, left standstill 80～120 minutes, and pumped into centrifugal device then, the liquid that liquid that proportion is bigger and needed proportion are lighter in centrifugal device separates, after the separation light liquid is sent into vaporizer, in vaporizer, alcohols is evaporated, separate with alcohol ester, be transmitted back to again in the alcohols hold-up vessel through cooling again; Alcohol ester-be biofuel flows in the storage tank standby through adding heat extraction moisture; Alcohols is methyl alcohol or ethanol.All devices is fixed on one and movably equips, and on automobile, panzer, interconnects by pipeline, valve, pump between the equipment; The raw material pipeline by valve respectively with the catalyst reaction jar, the alcohols hold-up vessel, the outlet of animal-plant oil jar connects, the other end of raw material pipeline is connected to respectively in the hybrid reaction jar of sealing, in the hybrid reaction jar whipping appts is arranged, reflux and heating unit, one the band valve pipeline with the hybrid reaction jar with leave standstill the jar be connected, leaving standstill jar is connected with the high speed centrifugation device by in-line pump, the liquid exit of centrifugal device, be connected with evaporation unit by in-line pump, evaporation unit has can be for the outlet of alcohols gas, and get back to the alcohols hold-up vessel by refrigerating unit and pipeline, have on the evaporation unit for the effusive outlet of alcohol ester, and be connected with storage tank by valve, also have jettison gear on the storage tank; Heating unit in the hybrid reaction jar can utilize the electric energy of generator car to heat, and the tail gas in the time of also can utilizing automobile, panzer work heats after heat exchange.
The invention has the beneficial effects as follows, the production of this biofuel, because the process time is shorter, equipment all is installed in one again and movably equips, therefore become movably energy resource supply base station, can make things convenient for mobile bigger industry such as army, geological prospecting, road and rail construction.
Description of drawings
Accompanying drawing 1 is a main technique flow process of the present invention.
Accompanying drawing 2 is one-piece construction synoptic diagram of the present invention.
Among the figure: running gear (1), fuel-displaced device (2), storage tank (3), alcohols reclaims mouthful (4), vaporizer (5), vegetable and animals oils hold-up vessel (6), catalyst preparation tank (7), alcohols hold-up vessel (8), hybrid reaction jar (9), whipping appts (10), heating unit (11), reflux (12), interchanger (13) leaves standstill jar (14), in-line pump (15), centrifugal device (16), in-line pump (17), diesel oil output channel (18).
Specific embodiments.
Fig. 2 is embodiments of the invention, and running gear (1) is an automobile, and Fig. 1 is the technical process of embodiment.Technical process is mainly by running gear (1), fuel-displaced device (2), storage tank (3), alcohols reclaims mouthful (4), vaporizer (5), vegetable and animals oils hold-up vessel (6), catalyst preparation tank (7), alcohols hold-up vessel (8), hybrid reaction jar (9), whipping appts (10), heating unit (11), reflux (12), interchanger (13) leaves standstill jar (14), in-line pump (15), centrifugal device (16), in-line pump (17), diesel oil output channel (18) is formed.All devices all is installed on the platform of automobile, interconnects by pipeline, valve or in-line pump; The raw material pipeline by valve respectively with catalyst preparation tank (7), alcohols hold-up vessel (8), the outlet of vegetable and animals oils hold-up vessel (6) connects, the other end of raw material pipeline is connected to respectively in the hybrid reaction jar (9) of sealing, whipping appts (10) is arranged in the hybrid reaction jar (9), heating unit (11) and reflux (12), one the band valve pipeline with hybrid reaction jar (9) with leave standstill the jar (14) be connected, leaving standstill jar (14) is connected with centrifugal device (16) by in-line pump (15), the liquid exit of centrifugal device (16), be connected with evaporation unit (5) by in-line pump (17), evaporation unit (5) has alcohols to reclaim mouthful (4), the alcohols that recycles and reuses, get back to alcohols hold-up vessel (8) by refrigerating unit and pipeline, have on the evaporation unit (5) for the effusive outlet of alcohol ester, and be connected with storage tank (3) by valve, also have fuel-displaced device (2) on the storage tank (3); Heating unit (11) in the hybrid reaction jar (9) can utilize the electric energy of generator car to heat, and the tail vapour in the time of also can utilizing automobile, panzer work heats after heat exchange.
The vegetable and animals oils of collecting is placed in the vegetable and animals oils hold-up vessel (6), stand-by through agitation and filtration; This two classes oil, available manufactured processed oil, the also waste product oil that can abandon with processed finished products when oil, or even the waste oil of used or corrupt high acid value; In catalyst preparation tank (7), prepare weakly alkaline composite catalyst, at first with organic sulfite and highly basic (NaOH) according to the kind of collecting oil, by weight: 1: 3～12 ratio feeds intake, in catalyst preparation tank (7), even through stirring thorough mixing, get weakly alkaline composite catalyst; Then with vegetable and animals oils hold-up vessel (6), alcohols hold-up vessel (8), the raw material of catalyst preparation tank (7), by weight percentage: 100: 10～50: 0.5～5 feed intake, three kinds of raw materials are entered in the hybrid reaction jar (9), under 50～100 ℃ temperature of reaction, through stirring, and after reflux (12) effect, compound is placed airtight leaving standstill in jar (14), left standstill 80～120 minutes, by in-line pump (15) mixed solution is pumped into centrifugal device (16) then, in centrifugal device (16) lining, the liquid that proportion is bigger separates than light liquid with required proportion, separate the back and send into evaporation unit (5) than light liquid, in evaporation unit (5), alcohols is evaporated, separate with alcohol ester, be transmitted back to again in the alcohols hold-up vessel (8) through cooling again; Alcohol ester-be biofuel flows in the storage tank (3) standby through adding heat extraction moisture; Alcohols is methyl alcohol or ethanol.
Claims (5)
1. mobile biodiesel producing base station, mainly by running gear, fuel-displaced device, storage tank, evaporation unit vegetable and animals oils hold-up vessel, catalyst preparation tank, the alcohols hold-up vessel, the hybrid reaction jar, heating unit leaves standstill jar, and equipment such as centrifugal device are formed; It is characterized in that composite catalyst by alkaline organic sulfite and highly basic by weight 1: 3～12, in catalyst preparation tank, prepare; Vegetable and animals oils, alcohols and composite catalyst 100: 10 by weight percentage～50: 0.5～5 is in the hybrid reaction jar, and under 50～100 ℃ temperature, stir, after the backflow, again in airtight leaving standstill in the jar, left standstill 80～120 minutes, by centrifugal device liquid and the lighter liquid separation of proportion that proportion is bigger, separate the lighter liquid of back proportion in evaporation unit, be separated into alcohols and alcohol ester once more; Equipment is installed in movably to be equipped on the platform, interconnects by pipeline, valve and in-line pump.
2. mobile biodiesel producing base station according to claim 1, it is characterized in that the raw material pipeline is connected with the outlet of catalyst preparation tank, alcohols hold-up vessel, vegetable and animals oils hold-up vessel respectively by valve, the other end of raw material pipeline is connected in the hybrid reaction jar of sealing, the band valve pipeline with the hybrid reaction jar with leave standstill the jar be connected, leaving standstill jar is connected with centrifugal device by in-line pump, the liquid exit of centrifugal device, be connected with evaporation unit by in-line pump, evaporation unit has alcohols to reclaim mouth and alcohol ester spout, and is connected with storage tank by valve.
3. mobile biodiesel producing base station according to claim 1 is characterized in that whipping appts, reflux and heating unit are arranged in the hybrid reaction jar.
4. mobile biodiesel producing base station according to claim 1 is characterized in that the heating unit in the hybrid reaction jar, can be electric energy, the tail vapour in the time of also can being automobile, panzer work, the heat energy after heat exchange.
5. mobile biodiesel producing base station according to claim 1 is characterized in that having flexible movement, and some movably install can be loaded in automobile, panzer, train, steamer etc.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2006101122321A CN101134903A (en) | 2006-08-31 | 2006-08-31 | Mobile biodiesel producing base station |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2006101122321A CN101134903A (en) | 2006-08-31 | 2006-08-31 | Mobile biodiesel producing base station |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101134903A true CN101134903A (en) | 2008-03-05 |
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ID=39159232
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA2006101122321A Pending CN101134903A (en) | 2006-08-31 | 2006-08-31 | Mobile biodiesel producing base station |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101134903A (en) |
Cited By (4)
| 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 |
| CN102918691A (en) * | 2010-03-31 | 2013-02-06 | 株式会社爱考斯研究 | Catalyst production method and device for same, and characteristic control method of a fuel cell reaction layer using catalyst |
| WO2013082048A1 (en) * | 2011-11-28 | 2013-06-06 | Revolution Fuels, Inc. | Methods and systems for converting food waste oil into biodiesel fuel |
| CN111303946A (en) * | 2019-12-02 | 2020-06-19 | 江西艾迪尔新能源有限公司 | High-cleanness high-efficiency biodiesel production device |
-
2006
- 2006-08-31 CN CNA2006101122321A patent/CN101134903A/en active Pending
Cited By (6)
| 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 |
| CN102918691A (en) * | 2010-03-31 | 2013-02-06 | 株式会社爱考斯研究 | Catalyst production method and device for same, and characteristic control method of a fuel cell reaction layer using catalyst |
| CN102918691B (en) * | 2010-03-31 | 2016-05-11 | 株式会社爱考斯研究 | The characteristic control method of conversion zone for the fuel cell of the manufacture method of catalyst and device thereof and employing catalyst |
| WO2013082048A1 (en) * | 2011-11-28 | 2013-06-06 | Revolution Fuels, Inc. | Methods and systems for converting food waste oil into biodiesel fuel |
| CN111303946A (en) * | 2019-12-02 | 2020-06-19 | 江西艾迪尔新能源有限公司 | High-cleanness high-efficiency biodiesel production device |
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Open date: 20080305 |