CN106833767A - A kind of biodiesel - Google Patents
A kind of biodiesel Download PDFInfo
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- CN106833767A CN106833767A CN201710247835.0A CN201710247835A CN106833767A CN 106833767 A CN106833767 A CN 106833767A CN 201710247835 A CN201710247835 A CN 201710247835A CN 106833767 A CN106833767 A CN 106833767A
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/12—Inorganic compounds
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/12—Inorganic compounds
- C10L1/1216—Inorganic compounds metal compounds, e.g. hydrides, carbides
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
- C10L1/1828—Salts thereof
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/22—Organic compounds containing nitrogen
- C10L1/23—Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites
- C10L1/231—Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites nitro compounds; nitrates; nitrites
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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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Abstract
本发明提供了一种生物柴油,包括如下重量份的组分:植物油60‑150份,甲醇10‑40份,催化剂3‑10份,油酸2‑5份,脂肪酸1‑5份,结晶型盐3‑6份,硝酸异辛酯0.02‑0.06份。本发明配方简单,原料易得,技术易于推广,与常规柴油相比,本生物柴油具有良好的环保性能、润滑性能、燃烧性能、安全性能。The invention provides a biodiesel, comprising the following components by weight: 60-150 parts of vegetable oil, 10-40 parts of methanol, 3-10 parts of catalyst, 2-5 parts of oleic acid, 1-5 parts of fatty acid, crystal form 3-6 parts of salt, 0.02-0.06 parts of isooctyl nitrate. The formula of the invention is simple, the raw materials are easy to obtain, and the technology is easy to popularize. Compared with conventional diesel oil, the biodiesel has good environmental protection performance, lubricating performance, combustion performance and safety performance.
Description
技术领域technical field
本发明涉及燃料油技术领域,具体涉及一种生物柴油。The invention relates to the technical field of fuel oil, in particular to biodiesel.
背景技术Background technique
日常使用的柴油是从不可再生资源石油中提炼的,石油日渐枯竭,寻找可替代燃料是必行趋势。石化柴油的燃烧不可避免会产生有害物质排放,而生物柴油是清洁的绿色能源,它是从生物质原料转变而来的。大力发展生物柴油对环境保护、减少石油依赖具有重大的战略意义。目前市场上大多数的生物柴油生产工艺复杂,制备设备要求较高,不易实现推广。Daily diesel oil is extracted from non-renewable petroleum resources. As petroleum is depleted day by day, finding alternative fuels is an inevitable trend. The combustion of petrochemical diesel will inevitably produce harmful emissions, while biodiesel is a clean and green energy source, which is transformed from biomass raw materials. Vigorously developing biodiesel is of great strategic significance to environmental protection and reducing oil dependence. At present, most of the biodiesel production processes in the market are complicated, and the requirements for preparation equipment are relatively high, so it is difficult to realize promotion.
发明内容Contents of the invention
本发明的目的在于公开一种生物柴油,解决上述现有技术问题中的一个或者多个。The purpose of the present invention is to disclose a biodiesel to solve one or more of the above-mentioned problems in the prior art.
为实现上述目的,本发明提供了一种生物柴油,包括如下重量份的组分:植物油60-150份,甲醇10-40份,催化剂3-10份,油酸2-5份,脂肪酸1-5份,结晶型盐3-6份,硝酸异辛酯0.02-0.06份。所述植物油为茶籽油、棕榈油、桐籽油、稻米油、大豆油、玉米油、葵花籽油、棉籽油、花生油中的一种或多种。所述催化剂为氢氧化钠、氢氧化钾、甲醇钠的一种或多种。所述结晶型盐为硅酸盐或硅铝酸盐的一种或多种。To achieve the above object, the present invention provides a biodiesel, comprising the following components by weight: 60-150 parts of vegetable oil, 10-40 parts of methanol, 3-10 parts of catalyst, 2-5 parts of oleic acid, 1- 5 parts, 3-6 parts of crystalline salt, 0.02-0.06 parts of isooctyl nitrate. The vegetable oil is one or more of tea seed oil, palm oil, tung oil, rice oil, soybean oil, corn oil, sunflower oil, cottonseed oil, and peanut oil. The catalyst is one or more of sodium hydroxide, potassium hydroxide and sodium methoxide. The crystalline salt is one or more of silicate or aluminosilicate.
本发明具有如下有益效果:本发明配方简单,原料易得,技术易于推广,与常规柴油相比,本生物柴油具有良好的环保性能、润滑性能、燃烧性能、安全性能。The invention has the following beneficial effects: the formula of the invention is simple, the raw materials are easy to obtain, and the technology is easy to popularize. Compared with conventional diesel oil, the biodiesel has good environmental protection performance, lubricating performance, combustion performance and safety performance.
具体实施方式detailed description
下面结合各实施方式对本发明进行详细说明,但应当说明的是,这些实施方式并非对本发明的限制,本领域普通技术人员根据这些实施方式所作的功能、方法、或者结构上的等效变换或替代,均属于本发明的保护范围之内。The present invention will be described in detail below in conjunction with various embodiments, but it should be noted that these embodiments are not limitations of the present invention, and those of ordinary skill in the art can make functional, method, or structural equivalent transformations or replacements based on these embodiments. , all fall within the protection scope of the present invention.
实施例1Example 1
备料:包括如下重量份的组分:大豆油60份,甲醇10份,氢氧化钠3份,油酸2份,脂肪酸1份,硅酸盐3份,硝酸异辛酯0.02份。Preparation of raw materials: including the following components by weight: 60 parts of soybean oil, 10 parts of methanol, 3 parts of sodium hydroxide, 2 parts of oleic acid, 1 part of fatty acid, 3 parts of silicate, and 0.02 parts of isooctyl nitrate.
制备步骤及方法:Preparation steps and methods:
S1、将大豆油加入到具有搅拌设备的反应釜中,搅拌速度为330r/min,再加入油酸、脂肪酸、部分甲醇,室温下高速搅拌2h形成均匀的乳状液;S1. Add soybean oil into a reaction kettle with stirring equipment at a stirring speed of 330r/min, then add oleic acid, fatty acid, and part of methanol, and stir at high speed for 2 hours at room temperature to form a uniform emulsion;
S2、在上述乳状液中加入硅酸盐,高速搅拌2h;S2, adding silicate to the above emulsion, stirring at high speed for 2 hours;
S3、将氢氧化钠溶于剩余的甲醇中,加入到S2的乳状液中,在65℃下回流反应1h;S3. Sodium hydroxide is dissolved in the remaining methanol, added to the emulsion of S2, and refluxed at 65° C. for 1 hour;
S4、反应完成后,将反应物料降温至40℃,进行静置分离,分离下层的甘油等副产物,得生物柴油粗品;S4. After the reaction is completed, the temperature of the reaction material is lowered to 40° C., and static separation is carried out to separate by-products such as glycerin in the lower layer to obtain crude biodiesel;
S5、再经过分子蒸馏,加入硝酸异辛酯,制得达标的生物柴油。S5. After molecular distillation, isooctyl nitrate is added to obtain standard biodiesel.
实施例2Example 2
备料:包括如下重量份的组分:大豆油30份,菜籽油50份,稻米油30份,甲醇35份,氢氧化钠3份,氢氧化钾2份,甲醇钠2份,油酸4份,脂肪酸3份,硅酸盐3份,硅铝酸盐2份,硝酸异辛酯0.04份。Material preparation: including the following components by weight: 30 parts of soybean oil, 50 parts of rapeseed oil, 30 parts of rice oil, 35 parts of methanol, 3 parts of sodium hydroxide, 2 parts of potassium hydroxide, 2 parts of sodium methoxide, 4 parts of oleic acid 3 parts, 3 parts of fatty acid, 3 parts of silicate, 2 parts of aluminosilicate, 0.04 part of isooctyl nitrate.
制备步骤及方法:Preparation steps and methods:
S1、将大豆油、菜籽油、稻米油加入到具有搅拌设备的反应釜中,搅拌速度为330r/min,再加入油酸、脂肪酸、部分甲醇,室温下高速搅拌2h形成均匀的乳状液;S1. Add soybean oil, rapeseed oil, and rice oil into a reaction kettle with stirring equipment at a stirring speed of 330r/min, then add oleic acid, fatty acid, and part of methanol, and stir at high speed for 2 hours at room temperature to form a uniform emulsion;
S2、在上述乳状液中加入硅酸盐、硅铝酸盐,高速搅拌2h;S2. Add silicate and aluminosilicate to the above emulsion, and stir at high speed for 2 hours;
S3、将氢氧化钠、氢氧化钾、甲醇钠溶于剩余的甲醇中,加入到S2的乳状液中,在65℃下回流反应1h;S3. Sodium hydroxide, potassium hydroxide, and sodium methoxide are dissolved in the remaining methanol, added to the emulsion of S2, and refluxed at 65° C. for 1 hour;
S4、反应完成后,将反应物料降温至40℃,进行静置分离,分离下层的甘油等副产物,得生物柴油粗品;S4. After the reaction is completed, the temperature of the reaction material is lowered to 40° C., and static separation is carried out to separate by-products such as glycerin in the lower layer to obtain crude biodiesel;
S5、再经过分子蒸馏,加入硝酸异辛酯,制得达标的生物柴油。S5. After molecular distillation, isooctyl nitrate is added to obtain standard biodiesel.
实施例3Example 3
备料:包括如下重量份的组分:棕榈油50份,菜籽油50份,大豆油50份,甲醇40份,氢氧化钠5份,氢氧化钾3份,甲醇钠2份,油酸5份,脂肪酸5份,硅酸盐3份,硅铝酸盐3份,硝酸异辛酯0.06份。Raw materials: including the following components by weight: 50 parts of palm oil, 50 parts of rapeseed oil, 50 parts of soybean oil, 40 parts of methanol, 5 parts of sodium hydroxide, 3 parts of potassium hydroxide, 2 parts of sodium methoxide, 5 parts of oleic acid 5 parts, 5 parts of fatty acid, 3 parts of silicate, 3 parts of aluminosilicate, 0.06 part of isooctyl nitrate.
制备步骤及方法:Preparation steps and methods:
S1、将棕榈油、菜籽油、大豆油加入到具有搅拌设备的反应釜中,搅拌速度为330r/min,再加入油酸、脂肪酸、部分甲醇,室温下高速搅拌2h形成均匀的乳状液;S1. Add palm oil, rapeseed oil, and soybean oil to a reaction kettle with stirring equipment, and the stirring speed is 330r/min, then add oleic acid, fatty acid, and part of methanol, and stir at high speed for 2 hours at room temperature to form a uniform emulsion;
S2、在上述乳状液中加入硅酸盐、硅铝酸盐,高速搅拌2h;S2. Add silicate and aluminosilicate to the above emulsion, and stir at high speed for 2 hours;
S3、将氢氧化钠、氢氧化钾、甲醇钠溶于剩余的甲醇中,加入到S2的乳状液中,在65℃下回流反应1h;S3. Sodium hydroxide, potassium hydroxide, and sodium methoxide are dissolved in the remaining methanol, added to the emulsion of S2, and refluxed at 65° C. for 1 hour;
S4、反应完成后,将反应物料降温至40℃,进行静置分离,分离下层的甘油等副产物,得生物柴油粗品;S4. After the reaction is completed, the temperature of the reaction material is lowered to 40° C., and static separation is carried out to separate by-products such as glycerin in the lower layer to obtain crude biodiesel;
S5、再经过分子蒸馏,加入硝酸异辛酯,制得达标的生物柴油。S5. After molecular distillation, isooctyl nitrate is added to obtain standard biodiesel.
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1760343A (en) * | 2005-11-01 | 2006-04-19 | 泸天化(集团)有限责任公司 | Biologic diesel oil in alcohol group, and production technique |
CN101601993A (en) * | 2009-07-10 | 2009-12-16 | 中国农业科学院油料作物研究所 | A kind of solid base catalyst for transesterification and preparation method thereof |
CN102430426A (en) * | 2010-09-17 | 2012-05-02 | 赢创德固赛有限责任公司 | Catalyst system for biodiesel production |
CN103987689A (en) * | 2011-10-13 | 2014-08-13 | 巴斯夫公司 | Method for the preparation of esters |
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2017
- 2017-04-19 CN CN201710247835.0A patent/CN106833767A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1760343A (en) * | 2005-11-01 | 2006-04-19 | 泸天化(集团)有限责任公司 | Biologic diesel oil in alcohol group, and production technique |
CN101601993A (en) * | 2009-07-10 | 2009-12-16 | 中国农业科学院油料作物研究所 | A kind of solid base catalyst for transesterification and preparation method thereof |
CN102430426A (en) * | 2010-09-17 | 2012-05-02 | 赢创德固赛有限责任公司 | Catalyst system for biodiesel production |
CN103987689A (en) * | 2011-10-13 | 2014-08-13 | 巴斯夫公司 | Method for the preparation of esters |
Non-Patent Citations (1)
Title |
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李东光: "《实用化工产品配方与制备(九)》", 31 August 2013, 中国纺织出版社 * |
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