CN103804130A - Method for preparing policosanol through beeswax normal-pressure reduction method - Google Patents
Method for preparing policosanol through beeswax normal-pressure reduction method Download PDFInfo
- Publication number
- CN103804130A CN103804130A CN201210437994.4A CN201210437994A CN103804130A CN 103804130 A CN103804130 A CN 103804130A CN 201210437994 A CN201210437994 A CN 201210437994A CN 103804130 A CN103804130 A CN 103804130A
- Authority
- CN
- China
- Prior art keywords
- beeswax
- water
- add
- mass ratio
- organic solvent
- Prior art date
- 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.)
- Pending
Links
- 235000013871 bee wax Nutrition 0.000 title claims abstract description 44
- 239000012166 beeswax Substances 0.000 title claims abstract description 44
- 238000000034 method Methods 0.000 title claims abstract description 34
- 229960001109 policosanol Drugs 0.000 title 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 33
- 239000003960 organic solvent Substances 0.000 claims abstract description 14
- 239000012071 phase Substances 0.000 claims abstract description 13
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 9
- 230000007935 neutral effect Effects 0.000 claims abstract description 6
- 239000012074 organic phase Substances 0.000 claims abstract description 6
- 238000003756 stirring Methods 0.000 claims abstract description 6
- 239000002994 raw material Substances 0.000 claims abstract description 4
- 239000002904 solvent Substances 0.000 claims abstract description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 15
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 8
- -1 lithium aluminum hydride Chemical compound 0.000 claims description 8
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 6
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 6
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 6
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 6
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 4
- 239000012280 lithium aluminium hydride Substances 0.000 claims description 4
- 239000011541 reaction mixture Substances 0.000 claims description 3
- 125000004432 carbon atom Chemical group C* 0.000 claims description 2
- DNIAPMSPPWPWGF-GSVOUGTGSA-N (R)-(-)-Propylene glycol Chemical compound C[C@@H](O)CO DNIAPMSPPWPWGF-GSVOUGTGSA-N 0.000 claims 1
- 239000012153 distilled water Substances 0.000 claims 1
- 239000003651 drinking water Substances 0.000 claims 1
- 235000020188 drinking water Nutrition 0.000 claims 1
- 239000003921 oil Substances 0.000 claims 1
- 239000008399 tap water Substances 0.000 claims 1
- 235000020679 tap water Nutrition 0.000 claims 1
- 239000000203 mixture Substances 0.000 abstract description 11
- 238000006243 chemical reaction Methods 0.000 abstract description 5
- 208000012839 conversion disease Diseases 0.000 abstract description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 abstract 4
- 238000001816 cooling Methods 0.000 abstract 1
- 230000007613 environmental effect Effects 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
- 239000001993 wax Substances 0.000 description 8
- 150000002191 fatty alcohols Chemical class 0.000 description 7
- 235000014113 dietary fatty acids Nutrition 0.000 description 5
- 229930195729 fatty acid Natural products 0.000 description 5
- 239000000194 fatty acid Substances 0.000 description 5
- 150000002148 esters Chemical class 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 108090001060 Lipase Proteins 0.000 description 2
- 239000004367 Lipase Substances 0.000 description 2
- 102000004882 Lipase Human genes 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 150000001298 alcohols Chemical class 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- NOPFSRXAKWQILS-UHFFFAOYSA-N docosan-1-ol Chemical compound CCCCCCCCCCCCCCCCCCCCCCO NOPFSRXAKWQILS-UHFFFAOYSA-N 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 235000019421 lipase Nutrition 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 238000007127 saponification reaction Methods 0.000 description 2
- TYWMIZZBOVGFOV-UHFFFAOYSA-N tetracosan-1-ol Chemical compound CCCCCCCCCCCCCCCCCCCCCCCCO TYWMIZZBOVGFOV-UHFFFAOYSA-N 0.000 description 2
- 238000005809 transesterification reaction Methods 0.000 description 2
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000371 Esterases Proteins 0.000 description 1
- 239000004164 Wax ester Substances 0.000 description 1
- 210000001015 abdomen Anatomy 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000005903 acid hydrolysis reaction Methods 0.000 description 1
- 238000006136 alcoholysis reaction Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 159000000007 calcium salts Chemical class 0.000 description 1
- 239000007765 cera alba Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 229960000735 docosanol Drugs 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 210000005036 nerve Anatomy 0.000 description 1
- 230000008635 plant growth Effects 0.000 description 1
- 239000005648 plant growth regulator Substances 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 208000023958 prostate neoplasm Diseases 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000036299 sexual function Effects 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
- 235000019386 wax ester Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
- C07C29/136—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH
- C07C29/147—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of carboxylic acids or derivatives thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
本发明提供一种蜂蜡还原法制备高级烷醇的方法,其特征在于以蜂蜡为原料,不需要有机溶剂参与反应的条件下,于常压开放体系中还原制备高级烷醇混合物。在85~120℃、持续搅拌的条件下,用还原剂∶蜂蜡=1∶10~30的质量比进行反应;再按蜂蜡:水:有机溶剂=1:10~30:0~30的质量比加入水和有机溶剂,加热至45~96℃,按蜂蜡:HCl=1:0.1~0.9的质量比加入2M的HCl溶液,45~96℃保温10~30min;抽出水相,在有机相中加水和盐酸溶液45~96℃保温10~30min,调节pH值为中性;抽出水相,蒸干有机相中的溶剂,冷却后的固体即为高级烷醇的混合物。本发明具有工艺简洁、易于操作、环境友好安全、反应在常压开放体系中进行、成本低、反应转化率高、适宜工业化应用等优点。The invention provides a method for preparing higher alkanols by reducing beeswax, which is characterized in that beeswax is used as a raw material and the mixture of higher alkanols is prepared by reduction in an open system at normal pressure without the need for an organic solvent to participate in the reaction. Under the condition of 85~120℃ and continuous stirring, react with reducing agent: beeswax=1:10~30 mass ratio; then press beeswax:water:organic solvent=1:10~30:0~30 mass ratio Add water and organic solvent, heat to 45-96°C, add 2M HCl solution according to the mass ratio of beeswax:HCl=1:0.1-0.9, keep warm at 45-96°C for 10-30min; extract the water phase, add water to the organic phase Incubate with hydrochloric acid solution at 45-96°C for 10-30 minutes, adjust the pH value to be neutral; extract the water phase, evaporate the solvent in the organic phase, and the solid after cooling is a mixture of higher alkanols. The invention has the advantages of simple process, easy operation, environmental friendliness and safety, the reaction is carried out in an open system at normal pressure, low cost, high reaction conversion rate, suitable for industrial application and the like.
Description
技术领域 technical field
[0001] 本发明涉及一种蜂蜡制备高级烷醇混合物的方法,尤其是一种常压还原法制备高级烷醇混合物的方法。 The present invention relates to a kind of method that beeswax prepares higher alkanol mixture, especially a kind of method that normal pressure reduction method prepares higher alkanol mixture. the
背景技术 Background technique
[0002] 蜂蜡是由工蜂腹部分泌出的物质,有蜂蜡、白蜂蜡、中国蜂蜡等,蜂蜡熔点为 6 1~65 ℃,酸值16~23 mg KOH/g,酯值72~79,皂化值88~102 mg KOH/g,碘值8~11 g/100 g。蜂蜡主要成分为脂酸与长链脂肪醇所形成的高级酯,天然高级酯是制备高级烷醇的重要原料。 Beeswax is the material secreted by worker bee abdomen, has beeswax, white beeswax, Chinese beeswax etc., beeswax fusing point is 61~65 ℃, acid value 16~23 mg KOH/g, ester value 72~79, saponification value 88-102 mg KOH/g, iodine value 8-11 g/100 g. The main components of beeswax are higher esters formed by fatty acids and long-chain fatty alcohols. Natural higher esters are important raw materials for preparing higher alkanols. the
高级烷醇又称高级脂肪醇,是含有十二个碳原子以上的链状饱和一元醇。高级烷醇广泛存在于自然界中,但几乎不以天然游离的脂肪醇形式存在,而是以蜡酯的形式存在。国内外有关高级烷醇的研究集中在C22~C36混合醇的制备、分离及利用等技术领域。高级烷醇混合物中的二十二醇可用于抑制前列腺肿瘤;二十四醇可增强神经因子的机能;二十六醇具有神经保护和神经营养的作用;二十八醇是世界公认的抗疲劳物质,并具有降血脂和增强性功能等功效;三十醇是植物生长调节剂,具有促进植物生长的效果。目前由蜂蜡制备高级烷醇采用的方法有:(l)皂化法:将蜡在碱性条件下皂化分解并用钙盐沉淀去除脂肪酸盐后,再用溶剂萃取得到高级脂肪醇的混合物。该法工艺流程长,加上高级脂肪酸酯在水相中的溶解性和分散性比较差,所以得率较低,且产物纯度不高,由于该方法要用到大量的碱,不仅操作繁杂,而且还造成严重的环境污染等。(2) 酯交换法:将蜡进行醇解即酯交换反应,再根据反应产物的不同沸点,用真空蒸馏的方法,分离出不同的产物,从而得到高级脂肪醇的混合物的方法。该方法化学反应过程复杂,得到的反应产物种类较多,分离目的产品比较困难。(3)将蜡在酸性条件下进行水解,再经超临界流体浸出脂肪醇的方法。该方法中,因蜡的酸性水解是一个可逆反应,其平衡点又取决于水的比例和酯的性质,而蜡本身在水中的溶解度很小,因此,在酸性条件下,蜡很难分散到水中,所以水解这一步很难进行,得率较低。(4)先将蜡进行酶分解,之后再提取脂肪醇的方法。这种让蜡经脂肪酶或酯酶分解的方法,是一种很有前景的生物提取方法,可以在温和的条件下实现高级脂肪酸酯的水解,且脂肪酶最大的优势是它的选择性高,这包括位置选择性和脂肪酸酯的选择性,所以是今后发展的重要方向。但是目前由于分解蜡的酶不稳定,容易中毒失活,生产成本高,工艺条件不成熟,因此仍处于摸索性试验阶段,未得到产业化应用。 Higher alkanols, also known as higher fatty alcohols, are chain-like saturated monohydric alcohols containing more than twelve carbon atoms. Higher alkanols widely exist in nature, but hardly exist in the form of natural free fatty alcohols, but in the form of wax esters. The research on higher alkanols at home and abroad focuses on the technical fields of preparation, separation and utilization of C 22 ~C 36 mixed alcohols. Docosanol in the higher alkanol mixture can be used to inhibit prostate tumors; tetracosanol can enhance the function of nerve factors; substance, and has the effects of lowering blood fat and enhancing sexual function; triaicol is a plant growth regulator, which has the effect of promoting plant growth. At present, the methods used to prepare higher alkanols from beeswax are: (1) saponification: wax is saponified and decomposed under alkaline conditions, and after removing fatty acid salts with calcium salt precipitation, solvent extraction is used to obtain a mixture of higher fatty alcohols. The process of this method is long, and the solubility and dispersibility of higher fatty acid esters in the water phase are relatively poor, so the yield is low, and the product purity is not high. Because this method will use a large amount of alkali, not only the operation is complicated , but also cause serious environmental pollution. (2) Transesterification method: alcoholysis of wax, that is, transesterification reaction, and then according to the different boiling points of the reaction products, different products are separated by vacuum distillation to obtain a mixture of higher fatty alcohols. The chemical reaction process of this method is complicated, and there are many types of reaction products obtained, and it is difficult to separate the target product. (3) A method in which the wax is hydrolyzed under acidic conditions, and then the fatty alcohol is leached by a supercritical fluid. In this method, because the acidic hydrolysis of wax is a reversible reaction, its equilibrium point depends on the ratio of water and the nature of ester, and the solubility of wax itself in water is very small, therefore, under acidic conditions, wax is difficult to disperse to water, so the step of hydrolysis is difficult and the yield is low. (4) A method of enzymatically decomposing wax and then extracting fatty alcohol. This method of decomposing wax by lipase or esterase is a promising biological extraction method, which can realize the hydrolysis of higher fatty acid esters under mild conditions, and the biggest advantage of lipase is its selectivity High, which includes position selectivity and fatty acid ester selectivity, so it is an important direction for future development. However, due to the instability of wax-decomposing enzymes, easy poisoning and inactivation, high production costs, and immature process conditions, it is still in the stage of exploratory experiments and has not been applied industrially.
以上几种方法在制备高级烷醇方面均存在一些不足之处,但都是比较传统和常用的方法。以蜂蜡为原料经还原法制备高级烷醇混合物到目前还未见报道。 The above several methods all have some deficiencies in the preparation of higher alkanols, but they are all relatively traditional and commonly used methods. The preparation of higher alkanol mixtures by reduction method with beeswax as raw material has not been reported so far. the
发明内容 Contents of the invention
本发明的目的在于提供一种工艺简洁、易于操作、成本低、条件温和、环境友好、得率高的由蜂蜡制备高级烷醇混合物的方法。 The object of the present invention is to provide a method for preparing higher alkanol mixtures from beeswax with simple process, easy operation, low cost, mild conditions, environment-friendly and high yield. the
本发明通过下列技术方案完成:一种常压还原法制备蜂蜡高级烷醇混合物的方法,其特征在于经过下列步骤: The present invention is accomplished through the following technical solutions: a method for preparing beeswax higher alkanol mixtures by normal pressure reduction, characterized in that through the following steps:
A、将蜂蜡加热至83~120℃,持续搅拌的条件下,按还原剂∶蜂蜡=1∶10~30的质量比,将还原剂加入到蜂蜡中。 A. Heat the beeswax to 83-120° C., and add the reducing agent to the beeswax at a mass ratio of reducing agent:beeswax=1:10-30 under continuous stirring.
B、按照蜂蜡:水:有机溶剂=1:10~30:0~30的质量比在反应混合物中加入水和有机溶剂,加热至45~96 ℃,按蜂蜡:HCl=1:0.1~0.9的质量比加入2 M的HCl溶液,45~96 ℃保温10~30 min。 B. According to the mass ratio of beeswax: water: organic solvent = 1: 10 ~ 30: 0 ~ 30, add water and organic solvent to the reaction mixture, heat to 45 ~ 96 ℃, according to beeswax: HCl = 1: 0.1 ~ 0.9 Add 2 M HCl solution to the mass ratio, and keep warm at 45-96 °C for 10-30 min. the
C、抽出水相,加入蜂蜡15~30倍质量的水和少量2 M的HCl溶液,45~96 ℃保温10~30 min;之后用2 M NaOH溶液调节溶液的pH值至中性。 C. Pull out the water phase, add water 15-30 times the mass of beeswax and a small amount of 2 M HCl solution, keep it warm at 45-96 °C for 10-30 min; then use 2 M NaOH solution to adjust the pH value of the solution to neutral. the
D、抽出水相,蒸干有机相中的溶剂,冷却至常温,即得块状蜂蜡高级烷醇。 D. Take out the water phase, evaporate the solvent in the organic phase to dryness, and cool to normal temperature to obtain block beeswax higher alkanol. the
所述还原剂可以为Ranny-Ni、氢化铝锂;所述有机溶剂为乙醚、石油醚、甲醇、乙醇、氯仿、丙酮、乙酸乙酯、苯、丁醇等有机溶剂中的一种或几种。 The reducing agent can be Ranny-Ni, lithium aluminum hydride; the organic solvent is one or more of ether, petroleum ether, methanol, ethanol, chloroform, acetone, ethyl acetate, benzene, butanol and other organic solvents . the
本发明具有下列优点和效果:采用上述方案,即在较为温和的常压开放体系中,由蜂蜡制得高级烷醇混合物,不仅工艺简单,易于控制,而且反应过程无有机溶剂参与,环境友好安全,成本低,反应转化率高,产品质量好。 The present invention has the following advantages and effects: adopting the above-mentioned scheme, that is, in a relatively mild normal-pressure open system, a higher alkanol mixture is prepared from beeswax, which is not only simple in process and easy to control, but also without the participation of organic solvents in the reaction process, which is environmentally friendly and safe , low cost, high reaction conversion rate and good product quality. the
具体实施方式 Detailed ways
下面结合具体实施例对本发明做进一步描述。 The present invention will be further described below in conjunction with specific embodiments. the
实施例1 Example 1
A、在1000 ml烧杯中将100 g蜂蜡加热至85 ℃,持续搅拌的条件下,缓慢加入10 g还原剂Ranny-Ni。 A. Heat 100 g of beeswax to 85 °C in a 1000 ml beaker, and slowly add 10 g of reducing agent Ranny-Ni under continuous stirring.
B、在反应混合物中加入300 ml水,加热至96 ℃,加入2 M的HCl溶液150 ml,96 ℃保温20 min。 B. Add 300 ml of water to the reaction mixture, heat to 96 °C, add 150 ml of 2 M HCl solution, and keep at 96 °C for 20 min. the
C、抽出水相,加入300 ml水和2 M的HCl溶液5 ml,96 ℃保温10 min;之后用2 M NaOH溶液调节溶液的pH值至中性。 C. Pull out the water phase, add 300 ml of water and 5 ml of 2 M HCl solution, and keep warm at 96°C for 10 min; then use 2 M NaOH solution to adjust the pH value of the solution to neutral. the
D、抽出水相,冷却至常温,即得蜂蜡高级烷醇93 g。 D. Take out the water phase and cool to normal temperature to obtain 93 g of beeswax higher alkanol. the
实施例2 Example 2
A、在20 L烧瓶中将1000 g蜂蜡加热至90 ℃,持续搅拌的条件下,将80 g氢化铝锂加入到蜂蜡中。 A. Heat 1000 g of beeswax to 90 °C in a 20 L flask, and add 80 g of lithium aluminum hydride to the beeswax under continuous stirring.
B、在烧瓶中加入5 L水和2 L氯仿,加热至50 ℃,加入2 M的HCl溶液4 L,烧瓶接冷凝器50 ℃保温30 min。 B. Add 5 L of water and 2 L of chloroform into the flask, heat to 50 °C, add 4 L of 2 M HCl solution, and connect the flask to a condenser at 50 °C for 30 min. the
C、抽出水相,加入蜂蜡5 L水和2 M的HCl溶液100 ml,50 ℃保温10 min;之后用2 M NaOH溶液调节溶液的pH值至中性。 C. Pull out the water phase, add 5 L of beeswax water and 100 ml of 2 M HCl solution, and keep warm at 50 °C for 10 min; then adjust the pH value of the solution to neutral with 2 M NaOH solution. the
D、抽出水相,蒸干有机相中的有机溶剂,冷却至常温,得蜂蜡高级烷醇940 g。 D. Take out the water phase, evaporate the organic solvent in the organic phase to dryness, and cool to normal temperature to obtain 940 g of beeswax higher alkanol. the
实施例3 Example 3
A、在100 L反应釜中将15 kg蜂蜡加热至85 ℃,持续搅拌的条件下,缓慢加入氢化铝锂1.5 kg。 A. Heat 15 kg of beeswax to 85 °C in a 100 L reactor, and slowly add 1.5 kg of lithium aluminum hydride under continuous stirring.
B、往反应釜中加入35 L水、20 L石油醚、5 L丁醇,加热至55 ℃,加入2 M的HCl溶液10 L,55 ℃保温30 min。 B. Add 35 L of water, 20 L of petroleum ether, and 5 L of butanol into the reactor, heat to 55 °C, add 10 L of 2 M HCl solution, and keep at 55 °C for 30 min. the
C、抽出水相,加入30 L水和2 M的HCl溶液100 ml,80 ℃保温30 min;之后用2 M NaOH溶液调节溶液的pH值至中性。 C. Pull out the water phase, add 30 L of water and 100 ml of 2 M HCl solution, keep warm at 80 °C for 30 min; then adjust the pH value of the solution to neutral with 2 M NaOH solution. the
D、抽出水相,蒸干有机相中的有机溶剂,冷却至常温,即得块状蜂蜡高级烷醇14.1 kg。 D. Take out the water phase, evaporate the organic solvent in the organic phase to dryness, and cool to normal temperature to obtain 14.1 kg of block beeswax higher alkanol. the
Claims (4)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210437994.4A CN103804130A (en) | 2012-11-06 | 2012-11-06 | Method for preparing policosanol through beeswax normal-pressure reduction method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210437994.4A CN103804130A (en) | 2012-11-06 | 2012-11-06 | Method for preparing policosanol through beeswax normal-pressure reduction method |
Publications (1)
Publication Number | Publication Date |
---|---|
CN103804130A true CN103804130A (en) | 2014-05-21 |
Family
ID=50701573
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201210437994.4A Pending CN103804130A (en) | 2012-11-06 | 2012-11-06 | Method for preparing policosanol through beeswax normal-pressure reduction method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103804130A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106278815A (en) * | 2016-08-10 | 2017-01-04 | 湖北神农蜂语生物产业有限公司 | The method that Cera Flava prepares high triacontanol through reduction |
CN112500263A (en) * | 2020-12-07 | 2021-03-16 | 中国林业科学研究院资源昆虫研究所 | Method for preparing higher alkanol by reducing white wax with red aluminum under normal pressure |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101386562A (en) * | 2008-08-29 | 2009-03-18 | 中国林业科学研究院资源昆虫研究所 | Method for preparing policosanol mixture by nonsolvent reduction method |
-
2012
- 2012-11-06 CN CN201210437994.4A patent/CN103804130A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101386562A (en) * | 2008-08-29 | 2009-03-18 | 中国林业科学研究院资源昆虫研究所 | Method for preparing policosanol mixture by nonsolvent reduction method |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106278815A (en) * | 2016-08-10 | 2017-01-04 | 湖北神农蜂语生物产业有限公司 | The method that Cera Flava prepares high triacontanol through reduction |
CN112500263A (en) * | 2020-12-07 | 2021-03-16 | 中国林业科学研究院资源昆虫研究所 | Method for preparing higher alkanol by reducing white wax with red aluminum under normal pressure |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101386562B (en) | Method for preparing policosanol mixture by nonsolvent reduction method | |
CN101293811B (en) | Method for preparing advanced alkanol mixture with Chinese insect wax | |
CN103184245B (en) | Method for producing fatty acid by hydrolyzing lipid through three liquid-phase lipase catalytic systems | |
CN101195572A (en) | Method for synthesizing fatty acid methyl ester | |
CN105001297B (en) | A method for extracting phytosterols from plant asphalt | |
CN109721471B (en) | Method for purifying glycerin from by-product of biodiesel production | |
CN102807547B (en) | New process for extracting vitamin E and sterol from soybean oil deodorization distillate | |
CN106631753B (en) | Method for producing gallic acid by using superfine gallnut powder | |
CN107501098B (en) | Method for decoloring benzyl benzoate as heavy benzoic acid byproduct | |
CN103804130A (en) | Method for preparing policosanol through beeswax normal-pressure reduction method | |
CN103804125A (en) | Method for preparing policosanol through insect wax pressure reduction method | |
CN107216253A (en) | A kind of utilization enzyme-chemically United Technologies extract the production method of VE, sterol from soybean oil deodorizer distillate | |
CN103804128A (en) | Method for preparing high-grade alkanol from rice bran wax by reduction under pressure | |
CN103804126A (en) | Method for preparing high-grade alkanol by sorghum wax normal pressure reduction method | |
CN101412745B (en) | Improved method for extracting sterol from vegetable oil asphalt | |
CN105037133B (en) | A kind of method that nervonic acid is extracted from malania oleifera | |
CN101475444B (en) | Crude Glycerin Partial Dehydration Purification Process | |
CN103724191A (en) | Dimethyl malonate preparation method | |
CN103804137A (en) | Method used for preparing higher alkanols via rice bran wax normal pressure reduction | |
CN104211674A (en) | Industrialized production method for producing high-content natural vitamin E by utilizing hydrolysis reduction process | |
CN105481926A (en) | Method for directly preparing chenodeoxycholic acid from duck bile | |
CN103804135A (en) | Method used for preparing higher alkanols via sunflower wax normal pressure reduction | |
CN103724196A (en) | Dimethyl malonate preparation method | |
CN103804127A (en) | Method for preparing high-grade alkanol from sorghum wax by reduction under pressure | |
EP3068862B1 (en) | Method for producing soap from fatty and resin acids, and a soap composition thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20140521 |