CN104560409B - Method for direct preparation of biodiesel by utilizing microalgae ultrasonic-assisted ionic liquid composition - Google Patents
Method for direct preparation of biodiesel by utilizing microalgae ultrasonic-assisted ionic liquid composition Download PDFInfo
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- 239000002608 ionic liquid Substances 0.000 title claims abstract description 38
- 239000003225 biodiesel Substances 0.000 title claims abstract description 28
- 238000000034 method Methods 0.000 title claims abstract description 26
- 239000000203 mixture Substances 0.000 title claims abstract description 26
- 238000002360 preparation method Methods 0.000 title description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims abstract description 57
- 238000006243 chemical reaction Methods 0.000 claims abstract description 22
- 239000000706 filtrate Substances 0.000 claims abstract description 7
- 238000005292 vacuum distillation Methods 0.000 claims abstract description 7
- 239000012535 impurity Substances 0.000 claims abstract description 5
- 238000000227 grinding Methods 0.000 claims abstract description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 14
- 241000195493 Cryptophyta Species 0.000 claims description 9
- FHDQNOXQSTVAIC-UHFFFAOYSA-M 1-butyl-3-methylimidazol-3-ium;chloride Chemical compound [Cl-].CCCCN1C=C[N+](C)=C1 FHDQNOXQSTVAIC-UHFFFAOYSA-M 0.000 claims description 7
- 235000011187 glycerol Nutrition 0.000 claims description 6
- RVEJOWGVUQQIIZ-UHFFFAOYSA-N 1-hexyl-3-methylimidazolium Chemical compound CCCCCCN1C=C[N+](C)=C1 RVEJOWGVUQQIIZ-UHFFFAOYSA-N 0.000 claims description 4
- 241000195649 Chlorella <Chlorellales> Species 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 230000003068 static effect Effects 0.000 claims description 2
- KAIPKTYOBMEXRR-UHFFFAOYSA-N 1-butyl-3-methyl-2h-imidazole Chemical compound CCCCN1CN(C)C=C1 KAIPKTYOBMEXRR-UHFFFAOYSA-N 0.000 claims 1
- -1 compound ion Chemical class 0.000 claims 1
- 238000001816 cooling Methods 0.000 claims 1
- 238000004821 distillation Methods 0.000 claims 1
- 230000008030 elimination Effects 0.000 claims 1
- 238000003379 elimination reaction Methods 0.000 claims 1
- 239000004519 grease Substances 0.000 claims 1
- 229910052739 hydrogen Inorganic materials 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 claims 1
- 238000002156 mixing Methods 0.000 claims 1
- 125000004108 n-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 claims 1
- 150000003839 salts Chemical class 0.000 claims 1
- 238000012216 screening Methods 0.000 claims 1
- 238000002604 ultrasonography Methods 0.000 claims 1
- 238000000605 extraction Methods 0.000 abstract description 15
- 238000004519 manufacturing process Methods 0.000 abstract description 9
- 230000032050 esterification Effects 0.000 abstract description 5
- 238000005886 esterification reaction Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 4
- 230000003197 catalytic effect Effects 0.000 abstract description 3
- 238000004090 dissolution Methods 0.000 abstract description 2
- 238000001914 filtration Methods 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 30
- 235000019198 oils Nutrition 0.000 description 30
- 239000003960 organic solvent Substances 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000003786 synthesis reaction Methods 0.000 description 4
- 238000012546 transfer Methods 0.000 description 4
- TVCNKZCRZIIOOR-UHFFFAOYSA-M 1-hexyl-3-methylimidazol-3-ium;hydrogen sulfate Chemical compound OS([O-])(=O)=O.CCCCCC[N+]=1C=CN(C)C=1 TVCNKZCRZIIOOR-UHFFFAOYSA-M 0.000 description 3
- QVRCRKLLQYOIKY-UHFFFAOYSA-M 1-methyl-3-prop-2-enylimidazol-1-ium;chloride Chemical compound [Cl-].C[N+]=1C=CN(CC=C)C=1 QVRCRKLLQYOIKY-UHFFFAOYSA-M 0.000 description 3
- 102000004190 Enzymes Human genes 0.000 description 3
- 108090000790 Enzymes Proteins 0.000 description 3
- 241000195663 Scenedesmus Species 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 210000002421 cell wall Anatomy 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- 235000013305 food Nutrition 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000005809 transesterification reaction Methods 0.000 description 3
- 239000002028 Biomass Substances 0.000 description 2
- 239000002585 base Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 238000000638 solvent extraction Methods 0.000 description 2
- 238000013517 stratification Methods 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- RAXXELZNTBOGNW-UHFFFAOYSA-O Imidazolium Chemical compound C1=C[NH+]=CN1 RAXXELZNTBOGNW-UHFFFAOYSA-O 0.000 description 1
- 235000019484 Rapeseed oil Nutrition 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000003487 anti-permeability effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000002551 biofuel Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 210000000170 cell membrane Anatomy 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000006911 enzymatic reaction Methods 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 230000000243 photosynthetic effect Effects 0.000 description 1
- 239000003495 polar organic solvent Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000012429 reaction media Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/04—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils
- C11C3/10—Ester interchange
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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
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
- C11B1/106—Production of fats or fatty oils from raw materials by extracting using ultra-sounds
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- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/001—Refining fats or fatty oils by a combination of two or more of the means hereafter
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- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/008—Refining fats or fatty oils by filtration, e.g. including ultra filtration, dialysis
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- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
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- C11B3/00—Refining fats or fatty oils
- C11B3/12—Refining fats or fatty oils by distillation
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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
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- 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
本发明公开了一种微藻超声波辅助离子液体组合物直接制备生物柴油的方法,该方法包括以下步骤:a、将干燥的微藻除杂、粉碎、研磨后,过200~300目筛,取筛下物,加入离子液体组合物,混匀,然后加入甲醇,在超声辅助的条件下,60~110℃反应1~5小时;反应完全后的物料,室温下静置冷却1~1.5小时,经过滤去除微藻残渣后,滤液静止分层;取上层溶液进行减压蒸馏得粗生物柴油。该方法将离子液体溶解萃取性能、催化性能及超声波的空化效应相结合;将油脂的提取与油脂的酯化合二为一,操作简单方便,工艺步骤大大简化,能快速制备生物柴油,从而大大提高生产效率,降低生产成本,为工业化规模化生产生物柴油提供了一个新方法。
The invention discloses a method for directly preparing biodiesel from a microalgae ultrasonic-assisted ionic liquid composition. The method comprises the following steps: a. After removing impurities, crushing and grinding the dried microalgae, passing through a 200-300 mesh sieve, taking Add the ionic liquid composition to the undersize, mix well, then add methanol, and react at 60-110°C for 1-5 hours under the condition of ultrasonic assistance; after the complete reaction, let stand and cool at room temperature for 1-1.5 hours, After the microalgae residue is removed by filtration, the filtrate is statically stratified; the upper layer solution is taken and subjected to vacuum distillation to obtain crude biodiesel. The method combines the dissolution and extraction performance of ionic liquids, catalytic performance and the cavitation effect of ultrasonic waves; the extraction of oil and the esterification of oil are combined into one, the operation is simple and convenient, the process steps are greatly simplified, and biodiesel can be prepared quickly, thereby greatly Improve production efficiency, reduce production cost, and provide a new method for industrial scale production of biodiesel.
Description
技术领域:Technical field:
本发明涉及生物化工领域,具体涉及一种微藻超声波辅助离子液体组合物直接制备生物柴油的方法。The invention relates to the field of biochemical industry, in particular to a method for directly preparing biodiesel from an ionic liquid composition assisted by microalgae ultrasonic waves.
背景技术:Background technique:
石油资源的日益减少导致能源紧张和石油价格的飙升,使人们越来越关注寻找其替代品。生物柴油不仅燃烧性能与石油柴油相当,且具有环境友好,资源可再生的优点,是替代石油柴油的理想燃料,近年来备受关注。The dwindling oil resources lead to energy shortages and soaring oil prices, making people pay more and more attention to finding its substitutes. Biodiesel not only has the same combustion performance as petroleum diesel, but also has the advantages of environmental friendliness and renewable resources. It is an ideal fuel to replace petroleum diesel, and has attracted much attention in recent years.
目前,国外主要以菜籽油、大豆油为原料,采用强酸或强碱催化剂催化制备生物柴油。但联合国官方调查宣称美国和欧洲采用大量的粮食作物来生产生物燃料是导致全球粮食危机的重要原因,因此,积极寻找新的生物质原料,以缓解目前的粮食和能源危机已成为世界各国高度关注的问题。在众多的生物质中,藻类具有光合作用效率高、环境适应能力强、生长周期短、生物产量高的特点,因此藻类是制备生物质能源的良好材料。At present, foreign countries mainly use rapeseed oil and soybean oil as raw materials, and use strong acid or strong base catalysts to catalyze biodiesel production. However, the official investigation of the United Nations declared that the use of a large number of food crops in the United States and Europe to produce biofuels is an important cause of the global food crisis. Therefore, actively looking for new biomass raw materials to alleviate the current food and energy crisis has become a high concern for all countries in the world The problem. Among many biomasses, algae have the characteristics of high photosynthetic efficiency, strong environmental adaptability, short growth cycle and high biological yield, so algae are good materials for preparing biomass energy.
传统微藻生物柴油生产过程主要分为两个步骤:首先是采用有机溶剂从微藻原料中提取出油脂;然后,再将油脂送至反应容器中,通过强酸或强碱进行酯化反应。The traditional microalgae biodiesel production process is mainly divided into two steps: first, the oil is extracted from the microalgae raw material with an organic solvent; then, the oil is sent to a reaction vessel for esterification by strong acid or alkali.
发明内容:Invention content:
但传统工艺利用微藻制备生物柴油也存在亟待解决的问题:However, the traditional process of using microalgae to prepare biodiesel also has problems to be solved:
首先,由于大部分含油微藻细胞壁较厚,常规有机溶剂萃取时,细胞内的油脂难以渗出细胞壁,溶剂萃取油脂耗时长,而且需要耗用大量有机萃取剂,加大了分离的难度,且萃取效率低;另外用有机溶剂萃取后的微藻,需蒸馏出有机溶剂才能得到油脂。First of all, due to the thick cell wall of most oil-containing microalgae, it is difficult for the oil in the cell to seep out of the cell wall during conventional organic solvent extraction. Solvent extraction of oil takes a long time and requires a large amount of organic extractant, which increases the difficulty of separation The extraction efficiency is low; in addition, the microalgae extracted with an organic solvent need to distill off the organic solvent to obtain oil.
其次,传统工艺采用强酸或强碱制备生物柴油存在着醇消耗量大,产物难回收,环境污染大等缺点。利用酶法制备生物柴油,往往要在有机溶剂反应介质中进行,强极性的有机溶剂会夺取酶表面微环境中的必需水,严重影响酶反应活性,降低酶的使用寿命。Secondly, the traditional process of using strong acid or strong base to prepare biodiesel has the disadvantages of large alcohol consumption, difficult recovery of the product, and large environmental pollution. The preparation of biodiesel by enzymatic method is often carried out in the reaction medium of organic solvents. Strong polar organic solvents will deprive the necessary water in the microenvironment of the enzyme surface, seriously affect the activity of the enzyme, and reduce the service life of the enzyme.
针对上述待解决的技术问题,如若能将微藻油脂萃取与酯交换反应两部分耦合成一个单元,缩短工艺路线,并找到能够有效提高微藻油脂提取率和转化效率的反应体系,提高酯化合成量,对微藻生物柴油工业化制备,具有一定意义。In view of the above technical problems to be solved, if the two parts of microalgae oil extraction and transesterification reaction can be coupled into one unit, the process route can be shortened, and a reaction system that can effectively improve the extraction rate and conversion efficiency of microalgae oil can be found to improve the efficiency of esterification. The amount of synthesis has certain significance for the industrial production of microalgae biodiesel.
本发明的目的是提供一种微藻超声波辅助离子液体组合物直接制备生物柴油的方法。The purpose of the present invention is to provide a method for directly preparing biodiesel from microalgae ultrasonic-assisted ionic liquid composition.
本发明是通过以下技术方案予以实现的:The present invention is achieved through the following technical solutions:
一种微藻超声波辅助离子液体组合物直接制备生物柴油的方法,该方法包括以下步骤:A method for directly preparing biodiesel from a microalgae ultrasonic-assisted ionic liquid composition, the method comprising the following steps:
a、将干燥的微藻除杂、粉碎、研磨后,过200~300目筛,取筛下物,加入离子液体组合物,装入萃取-反应釜中,混匀,然后加入甲醇,在超声辅助的条件下,60~110℃反应1~5小时;所述离子液体组合物,由组分A和组分B混合组成,其中组分A质量分数为90%~98%,组分A选自1-丁基-3-甲基咪唑氯盐([BMIM]Cl)或1-烯丙基-3-甲基咪唑氯盐([AMIM]Cl),组分B选自1-丁基-3-甲基吗啉盐[Hnmm]Im或1-已基-3-甲基咪唑硫酸氢盐([HMIM]HSO4);所述微藻筛下物与复合离子液体组合物的质量比为1:10~1:40;所述甲醇与微藻油脂的摩尔比为6:1;a. After removing impurities, pulverizing and grinding the dried microalgae, pass through a 200-300 mesh sieve, take the sieve, add the ionic liquid composition, put it into the extraction-reaction kettle, mix well, then add methanol, Under auxiliary conditions, react at 60-110°C for 1-5 hours; the ionic liquid composition is composed of component A and component B, wherein the mass fraction of component A is 90%-98%, and component A is selected from From 1-butyl-3-methylimidazolium chloride ([BMIM]Cl) or 1-allyl-3-methylimidazolium chloride ([AMIM]Cl), component B is selected from 1-butyl- 3-methylmorpholine salt [Hnmm] Im or 1-hexyl-3-methylimidazolium bisulfate ([HMIM]HSO 4 ); the mass ratio of the microalgae undersize and the composite ionic liquid composition is 1:10~1:40; the molar ratio of methanol to microalgae oil is 6:1;
b、反应完全后的物料,室温下静置冷却1-1.5小时经过滤去除微藻残渣后,滤液静止分层;上层溶液进行减压蒸馏得粗生物柴油。b. After the reaction is complete, the material is allowed to stand and cool at room temperature for 1-1.5 hours, after filtering to remove the microalgae residue, the filtrate is statically stratified; the upper layer solution is subjected to vacuum distillation to obtain crude biodiesel.
所述的微藻选自小球藻或栅藻。The microalgae are selected from Chlorella or Scenedesmus.
步骤a所述超声,超声波功率为240W。The ultrasonic described in step a, the ultrasonic power is 240W.
步骤b静止分层后得到的下层溶液经蒸馏除去甲醇和甘油,回收离子液体,所述离子液体可循环使用。The lower layer solution obtained after static layering in step b is distilled to remove methanol and glycerin, and the ionic liquid is recovered, and the ionic liquid can be recycled.
本发明的有益效果如下:The beneficial effects of the present invention are as follows:
(1)本申请最大的特点是整个反应“一步完成”,也就是说,本申请专利以微藻粉为原料,微藻油脂的提取和微藻油脂转化为生物柴油同时进行,本方法将油脂的提取与油脂的酯化或转酯化工艺合二为一,避免了油脂的提取精炼,工艺步骤大大简化。(1) The biggest feature of this application is that the whole reaction is "one-step completion". The extraction and the esterification or transesterification process of oil are combined into one, which avoids the extraction and refining of oil and greatly simplifies the process steps.
(2)本申请的离子液体组合物不仅仅是用来催化微藻油脂生产生物柴油的,它还具有提取“微藻油脂”的作用,本申请的超声波不仅仅是用来辅助催化微藻油脂生产生物柴油的,它还具有辅助提取“微藻油脂”的作用,这样就实现了微藻油脂的提取,同时提取出来的微藻油脂直接转化为生物柴油。(2) The ionic liquid composition of this application is not only used to catalyze the production of biodiesel from microalgae oil, but also has the function of extracting "microalgae oil". The ultrasonic wave of this application is not only used to assist in catalyzing microalgae oil For the production of biodiesel, it also has the function of assisting in the extraction of "microalgae oil", so that the extraction of microalgae oil is realized, and the extracted microalgae oil is directly converted into biodiesel.
总之,本发明提供了一种超声波结合复合离子液体组合物提取微藻油脂并催化制备生物柴油的新方法。该方法利用离子液体对微藻细胞壁较强的溶解性和对微藻油脂较高的催化活性,结合超声波对微藻细胞膜增透破碎作用和超声振动作用加速离子液体及藻粉运动,增加离子液体及藻粉相互碰撞接触机会,从而提高微藻油脂提取率和油脂转化率。该方法将将离子液体溶解萃取性能、催化性能及超声波的空化效应等优势特点相结合;将油脂的提取与油脂的酯化或转酯化工艺合二为一,设计巧妙,操作简单方便,避免了油脂的提取精炼,工艺步骤大大简化,能快速制备生物柴油,从而大大提高生产效率,降低生产成本,为工业化规模化生产生物柴油提供了一个新方法。In conclusion, the present invention provides a new method for extracting oil from microalgae and catalyzing the preparation of biodiesel by combining ultrasonic waves with a composite ionic liquid composition. This method utilizes the strong solubility of ionic liquids to microalgal cell walls and high catalytic activity to microalgal oils, combined with the anti-permeability and crushing effect of ultrasonic waves on microalgal cell membranes and the action of ultrasonic vibration to accelerate the movement of ionic liquids and algae powder, increasing the concentration of ionic liquids. and algae flour collide with each other, thereby improving the oil extraction rate and oil conversion rate of microalgae. This method combines the advantages of ionic liquid dissolution and extraction performance, catalytic performance and ultrasonic cavitation effect; it combines the oil extraction and oil esterification or transesterification process into one, with ingenious design and simple and convenient operation. The extraction and refining of oil is avoided, the process steps are greatly simplified, and biodiesel can be prepared quickly, thereby greatly improving production efficiency and reducing production costs, and providing a new method for industrial and large-scale production of biodiesel.
附图说明:Description of drawings:
图1是本发明工艺流程示意图。Fig. 1 is a schematic diagram of the process flow of the present invention.
具体实施方式:detailed description:
以下是对本发明的进一步说明,而不是对本发明的限制。The following is a further description of the present invention, rather than a limitation of the present invention.
实施例1:Example 1:
将干燥栅藻除杂,粉碎、研磨后过200目筛;取5克筛下物,加入50克离子液体组合物(所述离子液体组合物,由组分A和组分B混合组成,其中组分A质量分数为90%,组分A为1-丁基-3-甲基咪唑氯盐([BMIM]Cl),组分B为1-丁基-3-甲基吗啉盐[Hnmm]Im)在萃取-反应釜中混合均匀,然后加入甲醇(甲醇与微藻油脂的摩尔比为6:1),在超声波合成萃取仪上,设定反应温度为70℃,超声波功率为240W,开始水浴反应,反应1小时后,于室温下静置冷却1小时,过滤藻粉,滤液转入到分液漏斗中,静置分层后,取上层溶液进行减压蒸馏,即得生物柴油粗品0.129克;下层经常压蒸馏、减压蒸馏除去甲醇和甘油,回收离子液体,所述离子液体可循环使用。The dried Scenedesmus was removed, pulverized and ground, and passed through a 200-mesh sieve; 5 grams of sieves were taken, and 50 grams of ionic liquid composition was added (the ionic liquid composition was composed of component A and component B mixed, wherein Component A mass fraction is 90%, component A is 1-butyl-3-methylimidazolium chloride salt ([BMIM]Cl), component B is 1-butyl-3-methylmorpholine salt [Hnmm ] Im) mixed uniformly in the extraction-reactor, then add methanol (the mol ratio of methanol and microalgae oil is 6:1), on the ultrasonic synthesis extraction instrument, set the reaction temperature to be 70°C, and the ultrasonic power is 240W, Start the reaction in a water bath. After reacting for 1 hour, let it stand and cool at room temperature for 1 hour, filter the algae powder, transfer the filtrate into a separatory funnel, and after standing to separate layers, take the upper solution and carry out vacuum distillation to obtain crude biodiesel. 0.129 grams; the lower layer is distilled under normal pressure and under reduced pressure to remove methanol and glycerol, and reclaim the ionic liquid, which can be recycled.
实施例2Example 2
将干燥栅藻除杂,粉碎、研磨后过300目筛;取5克筛下物,加入100克离子液体组合物(所述离子液体组合物,由组分A和组分B混合组成,其中组分A质量分数为95%,组分A为1-丁基-3-甲基咪唑氯盐([BMIM]Cl),组分B为1-已基-3-甲基咪唑硫酸氢盐([HMIM]HSO4))在萃取-反应釜中混合均匀,然后加入甲醇(甲醇与微藻油脂的摩尔比为6:1),在超声波合成萃取仪上,设定反应温度为80℃,超声波功率为240W,开始水浴反应,反应2小时后,于室温下静置冷却1小时,过滤藻粉,滤液转入到分液漏斗中,静置分层后,取上层溶液进行减压蒸馏,即得生物柴油粗品0.158克;下层经常压蒸馏、减压蒸馏除去甲醇和甘油,回收离子液体,所述离子液体可循环使用。The dried Scenedesmus was removed, pulverized and ground, and passed through a 300-mesh sieve; 5 grams of sieves were taken, and 100 grams of ionic liquid composition was added (the ionic liquid composition was composed of component A and component B mixed, wherein Component A mass fraction is 95%, component A is 1-butyl-3-methylimidazolium chloride ([BMIM]Cl), component B is 1-hexyl-3-methylimidazolium bisulfate ( [HMIM]HSO 4 )) was mixed uniformly in the extraction-reaction kettle, and then methanol was added (the molar ratio of methanol to microalgae oil was 6:1). The power is 240W, start the water bath reaction, after 2 hours of reaction, let it stand and cool at room temperature for 1 hour, filter the algae powder, transfer the filtrate into the separatory funnel, after standing for stratification, take the upper layer solution and carry out vacuum distillation, that is 0.158 g of crude biodiesel was obtained; the lower layer was distilled under normal pressure and reduced pressure to remove methanol and glycerol, and the ionic liquid was recovered, and the ionic liquid could be recycled.
实施例3Example 3
将干燥小球藻除杂,粉碎、研磨后过200目筛;取5克筛下物,加入150克离子液体组合物(所述离子液体组合物,由组分A和组分B混合组成,其中组分A质量分数为95%,组分A为1-烯丙基-3-甲基咪唑氯盐([AMIM]Cl),组分B为1-丁基-3-甲基吗啉盐[Hnmm]Im)在萃取-反应釜中混合均匀,然后加入甲醇(甲醇与微藻油脂的摩尔比为6:1),在超声波合成萃取仪上,设定反应温度为90℃,超声波功率为240W,开始水浴反应,反应3小时后,于室温下静置冷却1小时,过滤藻粉,滤液转入到分液漏斗中,静置分层后,取上层溶液进行减压蒸馏,即得生物柴油粗品0.197克;下层经常压蒸馏、减压蒸馏除去甲醇和甘油,回收离子液体,所述离子液体可循环使用。Remove impurities from the dried chlorella, crush and grind it and pass through a 200-mesh sieve; take 5 grams of sieved material, add 150 grams of ionic liquid composition (the ionic liquid composition is composed of component A and component B mixed, The mass fraction of component A is 95%, component A is 1-allyl-3-methylimidazolium chloride ([AMIM]Cl), and component B is 1-butyl-3-methylmorpholine [Hnmm] Im) was mixed uniformly in the extraction-reactor, then methanol was added (the mol ratio of methanol to microalgae oil was 6:1), and on the ultrasonic synthesis extraction instrument, the set reaction temperature was 90°C, and the ultrasonic power was 240W, start the water bath reaction, after 3 hours of reaction, let it stand and cool at room temperature for 1 hour, filter the algae powder, transfer the filtrate into a separatory funnel, after standing for stratification, take the upper solution and carry out vacuum distillation to obtain biological 0.197 g of crude diesel oil; the lower layer was distilled under normal pressure and reduced pressure to remove methanol and glycerin, and the ionic liquid was recovered, and the ionic liquid could be recycled.
实施例4Example 4
将干燥小球藻除杂,粉碎、研磨后过300目筛;取5克与200克复合离子液体组合物(所述离子液体组合物,由组分A和组分B混合组成,其中组分A质量分数为98%,组分A为1-烯丙基-3-甲基咪唑氯盐([AMIM]Cl),组分B为1-已基-3-甲基咪唑硫酸氢盐([HMIM]HSO4))在萃取-反应釜中混合均匀,然后加入甲醇(甲醇与微藻油脂的摩尔比为6:1),在超声波合成萃取仪上,设定反应温度为100℃,超声波功率为240W,开始水浴反应,反应4小时后,于室温下静置冷却1小时,过滤藻粉,滤液转入到分液漏斗中,静置分层后,取上层溶液进行减压蒸馏,即得生物柴油粗品0.199克;下层经常压蒸馏、减压蒸馏除去甲醇和甘油,回收离子液体,所述离子液体可循环使用。The dried chlorella is removed from impurities, pulverized and ground and passed through a 300-mesh sieve; get 5 grams and 200 grams of the composite ionic liquid composition (the ionic liquid composition is composed of component A and component B, wherein component A mass fraction is 98%, component A is 1-allyl-3-methylimidazolium chloride ([AMIM]Cl), component B is 1-hexyl-3-methylimidazolium bisulfate ([ HMIM]HSO 4 )) Mix well in the extraction-reaction kettle, then add methanol (the molar ratio of methanol to microalgae oil is 6:1), set the reaction temperature to 100°C on the ultrasonic synthesis extractor, and the ultrasonic power 240W, start the water bath reaction, after 4 hours of reaction, let stand and cool at room temperature for 1 hour, filter the algae powder, transfer the filtrate into a separatory funnel, after standing for layers, take the upper solution and carry out vacuum distillation to obtain 0.199 g of biodiesel crude product; the lower layer is distilled under normal pressure and reduced pressure to remove methanol and glycerin, and recover the ionic liquid, which can be recycled.
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