CN103131481A - Biosynthetic fuel - Google Patents

Biosynthetic fuel Download PDF

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Publication number
CN103131481A
CN103131481A CN2011102717890A CN201110271789A CN103131481A CN 103131481 A CN103131481 A CN 103131481A CN 2011102717890 A CN2011102717890 A CN 2011102717890A CN 201110271789 A CN201110271789 A CN 201110271789A CN 103131481 A CN103131481 A CN 103131481A
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fuel
raw materials
biosynthesizing
making method
normal temperature
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CN103131481B (en
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柏富军
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Bai Fujun
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XIANGFAN TONGKANG INDUSTRIAL Co Ltd
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

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Abstract

The invention provides biosynthetic fuel which comprises the following raw materials by weight: 42.97% of methanol, 42.97% of ethanol, 11.73% of castor oil, 1.46% of sodium hydrogen sulfate, 0.29% of ion emulsifiers, 0.29% of cosolvents, and 0.29% of methylphenol; the method comprises the following steps: 1) weighing the raw materials according to the weight percents, putting the raw materials into a stirring tank, stirring and well mixing; 2) putting the well mixed mixture into a reaction vessel, heating to 350 DEG C; 3) removing gas from the heated mixture by a gas-liquid separator, adding the mixture into a catalytic tower, injecting 4 m3 hydrogen per 1000 kg, then cooling to normal temperature by a column tube device; 4) adding the mixture cooled to normal temperature into a finished product pot, adding ferrocene with an amount of 5% of the total amount, and reaching an octane number of 10% to obtain the biosynthetic fuel. According to the invention, the bio-fuel is synthesized by methanol and ethanol through a scientific method; the biosynthetic fuel has several advantages of high heat value, low pollution discharge, reasonable cost, easily-available raw materials, and the like, and is regenerable ideal synthetic energy.

Description

A kind of biosynthesizing fuel
Technical field
The present invention relates to a kind of synthol, specifically a kind of biosynthesizing fuel.
Background technology
Along with improving constantly of economy and standard of living; energy consumption constantly enlarges; non-renewable petroleum resources are day by day exhausted; its energy dilemma on the horizon; will affect and restrict the development of world economy; in order to satisfy the growing material life of people and Economic development needs; develop and develop new renewable energy source and become the task of top priority; countries in the world are being all that the reply energy dilemma strengthens input in science and technology and development research, particularly calorific value are high, the low renewable new forms of energy of discharging have become the urgent major issue that the mankind face.
Summary of the invention
The object of the invention is to solve the day by day exhausted present situation of the current energy, a kind of biosynthesizing fuel is provided, have that calorific value is high, low, the rational distinguishing feature of cost of discharging, is a kind of scientific and reasonable renewable synthol.
The present invention includes the methyl alcohol, ethanol, Viscotrol C and the hydrogen sulfate that use in synthol and receive, the technical scheme that adopts is:
Its formulation weight per-cent is as follows:
Figure BSA00000573529200011
Figure BSA00000573529200021
Another object of the present invention is to provide a kind of making method of above-mentioned biosynthesizing fuel, mainly divide following a few step to carry out:
1) above-mentioned raw materials being put into stirred pot together by weight feeding mixes;
2) compound that stirs is put into reactor and be heated to 350 ℃;
3) compound after heating is got rid of gas through gas-liquid separator, and liquid directly enters catalytic tower, then injects 4m by every 1000Kg 3Hydrogen, then be down to normal temperature by the tubulation device;
4) compound that will be down to normal temperature is sent into finished pot, add by 5% of total amount ferrocene and 10% octane value for biological synthol.
In above-mentioned making method:
Making method 1) time of stirring in is 5~10 minutes.
Making method 2) be heated to 350 ℃ in, its air pressure should reach 4 pressure.
Technique scheme that the present invention passes through, because the main component in raw material has adopted reproducible methyl alcohol and ethanol, and allocate a small amount of industrial chemicals into, synthesize by simple making of science again, produce thing fuel after testing, its fuel value can reach 1.1 ten thousand kilocalories, the quantity discharged of hydrocarbon polymer and an oxidation is extremely low, calorific value is with existing suitable with gasoline, can be applied directly in existing motor car engine and use as power fuel, raw material required for the present invention easily obtains, and making processes is simple, has fabulous popularizing application prospect.
Description of drawings
The invention will be further described below in conjunction with drawings and Examples.
Accompanying drawing is process flow diagram of the present invention.
Embodiment
Embodiment 1: calculate to make 500Kg biosynthesizing fuel, desired raw material precentagewise meter weight is as follows: methyl alcohol 42.97% 214.85Kg, ethanol 42.97% 214.85Kg, Viscotrol C 11.73% 58.65Kg, hydrogen sulfate are received 1.46% 7.3Kg, ionic emulsifying agent 0.29% 1.45Kg, solubility promoter 0.29% 1.45Kg, cresols 0.29% 1.45Kg
Making method is as follows:
1) above-mentioned raw materials being put into stirred pot together by weight feeding mixes;
2) compound that stirs is put into reactor and be heated to 350 ℃;
3) compound after heating is got rid of gas through gas-liquid separator, and liquid directly enters catalytic tower, then injects 4m by every 1000Kg 3Hydrogen, then be down to normal temperature by the tubulation device;
4) compound that will be down to normal temperature is sent into finished pot, add by 5% of total amount 500Kg ferrocene 25Kg and 10% octane value 50Kg for biological synthol.
In above-mentioned making processes, method 1) churning time in is 5 minutes, the method formula) in heating after press exhausted 4 pressure that reach.
Embodiment 2: calculate to make 1000Kg biosynthesizing fuel, desired raw material precentagewise meter weight is as follows: methyl alcohol 42.97% 429.7Kg, ethanol 42.97% 429.7Kg, Viscotrol C 11.73% 117.3Kg, hydrogen sulfate are received 1.46% 14.6Kg, ionic emulsifying agent 0.29% 2.9Kg, solubility promoter 0.29% 2.9Kg, cresols 0.29% 2.9Kg
Making method is as follows:
1) above-mentioned raw materials being put into stirred pot together by weight feeding mixes;
2) compound that stirs is put into reactor and be heated to 350 ℃;
3) compound after heating is got rid of gas through gas-liquid separator, and liquid directly enters catalytic tower, then injects 4m by every 1000Kg 3Hydrogen, then be down to normal temperature by the tubulation device;
4) compound that will be down to normal temperature is sent into finished pot, add by 5% of total amount 500Kg ferrocene 50Kg and 10% octane value 100Kg for biological synthol.
In above-mentioned making processes, method 1) churning time in is 8 minutes, the method formula) in heating after press exhausted 4 pressure that reach.
Embodiment 3: calculate to make 2000Kg biosynthesizing fuel, desired raw material precentagewise meter weight is as follows: methyl alcohol 42.97% 859.4Kg, ethanol 42.97% 859.4Kg, Viscotrol C 11.73% 234.6Kg, hydrogen sulfate are received 1.46% 29.2Kg, ionic emulsifying agent 0.29% 5.8Kg, solubility promoter 0.29% 5.8Kg, cresols 0.29% 5.8Kg
Making method is as follows:
1) above-mentioned raw materials being put into stirred pot together by weight feeding mixes;
2) compound that stirs is put into reactor and be heated to 350 ℃;
3) compound after heating is got rid of gas through gas-liquid separator, and liquid directly enters catalytic tower, then injects 4m by every 1000Kg 3Hydrogen, then be down to normal temperature by the tubulation device;
4) compound that will be down to normal temperature is sent into finished pot, add by 5% of total amount 500Kg ferrocene 100Kg and 10% octane value 200Kg for biological synthol.
In above-mentioned making processes, method 1) churning time in is 10 minutes, the method formula) in heating after press exhausted 4 pressure that reach.
The various device that the present invention uses in making processes all can adopt traditional chemical industry equipment to produce, related back-pressure still, and it is good should adopting autoclave.

Claims (4)

1. biosynthesizing fuel comprises that the methyl alcohol, ethanol, Viscotrol C and the hydrogen sulfate that use in synthol receive, and it is characterized in that:
Its formulation weight per-cent is as follows:
Figure FSA00000573529100011
2. the making method of a biosynthesizing fuel claimed in claim 1, its feature is being: described method minute following steps are carried out:
1) above-mentioned raw materials being put into stirred pot together by weight feeding mixes;
2) compound that stirs is put into reactor and be heated to 350 ℃;
3) compound after heating is got rid of gas through gas-liquid separator, and liquid directly enters catalytic tower, then injects 4m by every 1000Kg 3Hydrogen, then be down to normal temperature by the tubulation device;
4) compound that will be down to normal temperature is sent into finished pot, add by 5% of total amount ferrocene and 10% octane value for biological synthol.
3. the making method of biosynthesizing fuel according to claim 2, its feature is being: the time of stirring making method 1) is 5~10 minutes.
4. the making method of biosynthesizing fuel according to claim 2, its feature is being: be heated to 350 ℃ making method 2), its air pressure should reach 4 pressure.
CN201110271789.0A 2011-11-22 2011-11-22 A kind of biosynthesizing fuel Active CN103131481B (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107629823A (en) * 2016-07-18 2018-01-26 任卫国 A kind of environmentally friendly synthetic liquid fuel
CN108070411A (en) * 2016-11-18 2018-05-25 黄运国 A kind of novel energy-saving environment-friendly fuel
CN113186005A (en) * 2021-03-29 2021-07-30 叁久国际新能源科技有限公司 Civil energy-saving environment-friendly fuel and preparation method thereof

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1928035A (en) * 2006-10-23 2007-03-14 姜彬 Environmental protection energy-saving diesel oil
US20100037513A1 (en) * 2006-04-27 2010-02-18 New Generation Biofuels, Inc. Biofuel Composition and Method of Producing a Biofuel

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100037513A1 (en) * 2006-04-27 2010-02-18 New Generation Biofuels, Inc. Biofuel Composition and Method of Producing a Biofuel
CN1928035A (en) * 2006-10-23 2007-03-14 姜彬 Environmental protection energy-saving diesel oil

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107629823A (en) * 2016-07-18 2018-01-26 任卫国 A kind of environmentally friendly synthetic liquid fuel
CN108070411A (en) * 2016-11-18 2018-05-25 黄运国 A kind of novel energy-saving environment-friendly fuel
CN113186005A (en) * 2021-03-29 2021-07-30 叁久国际新能源科技有限公司 Civil energy-saving environment-friendly fuel and preparation method thereof

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