[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

CN101613639A - Preparation method of epoxidized oil under ultrasonic condition - Google Patents

Preparation method of epoxidized oil under ultrasonic condition Download PDF

Info

Publication number
CN101613639A
CN101613639A CN200910065464A CN200910065464A CN101613639A CN 101613639 A CN101613639 A CN 101613639A CN 200910065464 A CN200910065464 A CN 200910065464A CN 200910065464 A CN200910065464 A CN 200910065464A CN 101613639 A CN101613639 A CN 101613639A
Authority
CN
China
Prior art keywords
oil
vegetable oil
epoxidized
ultrasonic
acid
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.)
Granted
Application number
CN200910065464A
Other languages
Chinese (zh)
Other versions
CN101613639B (en
Inventor
刘国琴
韩立娟
李琳
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Henan University of Technology
Original Assignee
Henan University of Technology
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Henan University of Technology filed Critical Henan University of Technology
Priority to CN200910065464XA priority Critical patent/CN101613639B/en
Publication of CN101613639A publication Critical patent/CN101613639A/en
Application granted granted Critical
Publication of CN101613639B publication Critical patent/CN101613639B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Fats And Perfumes (AREA)
  • Medicines Containing Plant Substances (AREA)

Abstract

本发明涉及一种超声条件下环氧化油脂的制备方法,所述制备方法包括:a.取一定量的植物油于反应容器中,将反应容器置于超声设备中,边搅拌边加入甲酸(冰乙酸或甲酸与冰乙酸的混合物)与催化剂的混合液。调节体系的温度,缓慢滴加双氧水,同时开启超声,控制超声的频率和功率;滴加完毕后,调节体系温度,并在一定的反应频率、功率和反应时间内超声;反应完成后,降至室温,静置后去除下层,得到粗环氧化植物油;b.将a步骤得到的粗环氧化植物油转移至水洗设备中,进行水洗,静置后去除水层;c.将b步骤得到的液体转移到减压蒸馏装置中,减压蒸馏脱除水分,得到环氧化植物油产品。The present invention relates to a kind of preparation method of epoxidized grease under ultrasonic condition, described preparation method comprises: a. take a certain amount of vegetable oil in reaction container, place reaction container in ultrasonic equipment, add formic acid (ice) while stirring A mixture of acetic acid or formic acid and glacial acetic acid) and catalyst. Adjust the temperature of the system, slowly add hydrogen peroxide dropwise, and turn on the ultrasound at the same time to control the frequency and power of the ultrasound; At room temperature, remove the lower layer after standing still to obtain crude epoxidized vegetable oil; b. transfer the crude epoxidized vegetable oil obtained in step a to a water washing device, wash with water, and remove the water layer after standing; c. The liquid is transferred to a vacuum distillation device, and the moisture is removed by vacuum distillation to obtain an epoxidized vegetable oil product.

Description

超声条件下环氧化油脂的制备方法 Preparation method of epoxidized oil under ultrasonic condition

技术领域 technical field

本发明涉及一种环氧化油脂的制备方法,具体地说是涉及一种在超声条件下环氧化油脂的制备方法。该技术涉及声化学领域,也涉及环氧类增塑剂制备领域。The invention relates to a preparation method of epoxidized oil, in particular to a preparation method of epoxidized oil under ultrasonic conditions. The technology relates to the field of sonochemistry, and also relates to the field of epoxy plasticizer preparation.

背景技术 Background technique

增塑剂是重要的化工原料,广泛用于塑料、橡胶制品的加工。目前常用的增塑剂邻苯二甲酸酯为低分子物质,易使制品老化,有毒;而且随着石油危机的加剧,邻苯二甲酸酯的价格急剧升高。因此,采用可再生资源制备环境友好的增塑剂成为研究热点。环氧植物油是用精炼植物油采用过氧化物处理而制得的一种产品,适用于各种聚氯乙烯制品,各种食品包装材料,医用制品“输血袋”,各种薄膜、人造革、塑料壁纸及其他日用塑料制品,还可用于特种油墨,液体复合稳定剂等。其中聚氯乙烯户外使用的塑料制品、塑料膜等必须使用环氧植物油保证制品无毒、透明、耐热、耐低温、增韧、抗老化等。环氧植物油是世界上承认的无毒增塑剂,可作为食品药物的包装材料、玩具及家庭装饰材料的助剂。但是现有环氧植物油环氧值和环氧转化率低,环氧化反应时间长,不能满足发展的需要。Plasticizer is an important chemical raw material, which is widely used in the processing of plastic and rubber products. Currently commonly used plasticizers, phthalates, are low-molecular substances, which tend to age products and are toxic; and with the intensification of the oil crisis, the price of phthalates has risen sharply. Therefore, the use of renewable resources to prepare environmentally friendly plasticizers has become a research hotspot. Epoxy vegetable oil is a product obtained by treating refined vegetable oil with peroxide. It is suitable for various polyvinyl chloride products, various food packaging materials, medical products "blood transfusion bags", various films, artificial leather, plastic wallpapers And other daily-use plastic products, can also be used in special inks, liquid composite stabilizers, etc. Among them, the plastic products and plastic films used for PVC outdoors must use epoxy vegetable oil to ensure that the products are non-toxic, transparent, heat-resistant, low-temperature resistant, toughened, and anti-aging. Epoxy vegetable oil is a non-toxic plasticizer recognized in the world, and can be used as an auxiliary agent for food and drug packaging materials, toys and home decoration materials. However, the existing epoxy vegetable oil has low epoxy value and epoxy conversion rate, and the epoxidation reaction time is long, which cannot meet the needs of development.

很多学者已对环氧油脂的制备方法进行了研究,如中国专利申请号200810026739.4“一种环氧棕榈油增塑剂的生产方法”公开了一种环氧棕榈油增塑剂的生产方法,在不加任何溶剂的条件下,用棕榈油为原料,与环氧化剂在浓硫酸和/磷酸的催化作用下,在一定的温度、时间、配比等条件下合成环氧棕榈油增塑剂的方法。中国专利申请号200610085270.2“一种环氧菜籽油的制备方法”公开了将菜籽油与环氧化剂进行环氧化反应,生成环氧菜籽油的方法。中国专利申请号90105315.5“环氧油脂增塑剂的生产方法”则公开了在不加任何溶剂的条件下,用棉籽油或大豆油为原料,与低浓度的双氧水、冰醋酸和浓硫酸,在一定的温度、时间、配比等条件下合成环氧油脂增塑剂的方法。但是以上所述专利文献所公开的方法均存在进行环氧化反应的时间过长,环氧值和环氧转化率低的不足之处。因此,寻求一种更好的环氧油脂的制备方法是非常必要的。Many scholars have carried out research on the preparation method of epoxy grease, as Chinese patent application number 200810026739.4 " a kind of production method of epoxy palm oil plasticizer " discloses a kind of production method of epoxy palm oil plasticizer, in Under the condition of not adding any solvent, use palm oil as raw material, and under the catalysis of concentrated sulfuric acid and/phosphoric acid with epoxy oxidizing agent, the method for synthesizing epoxy palm oil plasticizer under certain conditions such as temperature, time, proportioning etc. . Chinese Patent Application No. 200610085270.2 "A Preparation Method of Epoxy Rapeseed Oil" discloses a method of epoxidizing rapeseed oil with an epoxidizing agent to generate epoxidized rapeseed oil. Chinese Patent Application No. 90105315.5 "Production Method of Epoxy Grease Plasticizer" discloses that under the condition of not adding any solvent, cottonseed oil or soybean oil is used as raw material, and hydrogen peroxide, glacial acetic acid and concentrated sulfuric acid of low concentration are used in A method for synthesizing epoxy grease plasticizer under certain temperature, time, proportioning and other conditions. However, the methods disclosed in the above-mentioned patent documents all have the disadvantages that the time for the epoxidation reaction is too long, and the epoxy value and the epoxy conversion rate are low. Therefore, it is very necessary to seek a better preparation method of epoxy grease.

发明内容 Contents of the invention

本发明的目的正是针对上述现有技术中所存在的不足之处而提供一种在超声条件下环氧化油脂的制备方法。该方法主要利用超声的空化作用、机械作用和超混合作用来加速植物油的环氧化反应,与现有技术相比不失为一种快速制备环氧化植物油的方法,且通过该方法可得到环氧值和环氧转化率均较高的环氧植物油产品,具有很好的经济可行性。The purpose of the present invention is just to provide a kind of preparation method of epoxidized grease under the ultrasonic condition in view of the deficiencies existing in the above-mentioned prior art. This method mainly utilizes ultrasonic cavitation, mechanical action and super-mixing action to accelerate the epoxidation reaction of vegetable oil. The epoxy vegetable oil product with high oxygen value and epoxy conversion rate has good economic feasibility.

本发明的目的可通过下述技术措施来实现:The purpose of the present invention can be achieved through the following technical measures:

本发明的在超声条件下环氧化油脂的制备方法包括以下步骤:The preparation method of epoxidized grease under ultrasonic condition of the present invention comprises the following steps:

a、取一定量的植物油置于反应容器中,再将反应容器置于超声设备中;a. Take a certain amount of vegetable oil and place it in a reaction vessel, and then place the reaction vessel in an ultrasonic device;

b、取a步骤所取植物油体积的10%~25%的甲酸、冰乙酸或甲酸与冰乙酸的混合物,以及a步骤所取植物油体积的0.75%~1.05%的催化剂进行搅拌混合,制备成混合液;B, take 10%~25% formic acid, glacial acetic acid or the mixture of formic acid and glacial acetic acid of the volume of vegetable oil taken in step a, and the catalyst of 0.75%~1.05% of the volume of vegetable oil taken in step a, stir and mix, and prepare the mixture liquid;

c、将b步骤所制备的混合液边搅拌边加入到a步骤的反应容器中;c, adding the mixed solution prepared in step b into the reaction vessel of step a while stirring;

d、调节体系的温度后开启超声设备,同时开始向c步骤所得体系中缓慢滴加双氧水,控制超声的频率和功率;滴加双氧水时体系的温度为35℃~60℃,滴加的双氧水体积为所取植物油体积的30%~70%,超声的频率为28kHz~100kHz,超声功率为120w~300w;d. After adjusting the temperature of the system, turn on the ultrasonic equipment, and at the same time start to slowly add hydrogen peroxide to the system obtained in step c, and control the frequency and power of the ultrasonic; 30% to 70% of the volume of the vegetable oil taken, the frequency of ultrasound is 28kHz to 100kHz, and the power of ultrasound is 120w to 300w;

e、双氧水滴加完毕后,再次调节体系温度至50℃~75℃,并在超声频率为28kHz~100kHz,超声功率为120w~300w,时间为15min~75min条件下进行环氧化反应;反应完成后,降至室温,静置后去除下层,得到粗环氧化植物油;e. After the addition of hydrogen peroxide is completed, adjust the temperature of the system again to 50°C-75°C, and carry out the epoxidation reaction under the conditions of ultrasonic frequency of 28kHz-100kHz, ultrasonic power of 120w-300w, and time of 15min-75min; the reaction is completed Afterwards, be down to room temperature, remove lower layer after leaving standstill, obtain crude epoxidized vegetable oil;

f、将e步骤得到的粗环氧化植物油转移至水洗设备中,进行水洗,静置后去除水层;f, transfer the crude epoxidized vegetable oil obtained in step e to water washing equipment, wash with water, and remove the water layer after standing;

g、将f步骤得到的液体转移到减压蒸馏装置中,减压蒸馏脱除水分,得到环氧化植物油产品。g. Transfer the liquid obtained in step f to a vacuum distillation device, and remove moisture by vacuum distillation to obtain an epoxidized vegetable oil product.

本发明中所述的催化剂为硫酸、磷酸、硬脂酸、油酸、硫酸铝、氯磺酸、酒石酸、杂多酸中的一种或一种以上;所述的植物油是大豆油、红花油、向日葵油、亚麻油、蓖麻油、菜籽油、桐油、棕榈油、花生油、脱水蓖麻油中的一种或一种以上混合物;所述的双氧水的质量百分比浓度为30%~80%。The catalyst described in the present invention is one or more of sulfuric acid, phosphoric acid, stearic acid, oleic acid, aluminum sulfate, chlorosulfonic acid, tartaric acid, heteropoly acid; the vegetable oil is soybean oil, safflower oil, sunflower oil, linseed oil, castor oil, rapeseed oil, tung oil, palm oil, peanut oil, dehydrated castor oil, or a mixture of more than one; the mass percent concentration of the hydrogen peroxide is 30% to 80%.

本发明的有益效果如下:The beneficial effects of the present invention are as follows:

由于超声有明显的空化效应,空化泡崩溃时产生的瞬间局部高温和高压可以加速化学反应;在液-液反应体系中,超声的机械作用和超混合效应可以使液-液相混合,形成很细小的乳化液,增加了相间接触从而加速化学反应,这些可能就是超声能加速植物油的环氧化反应的原因。因此本发明也正是利用了超声特有的这些效应,首次利用超声条件来制备环氧植物油,可同时提高环氧化植物油的环氧值和环氧转化率,同时缩短了环氧化反应的时间,与未使用超声条件相比环氧化反应时间缩短了70%~90%,可以减少运行费用,从而使本发明经济性更好。Due to the obvious cavitation effect of ultrasound, the instantaneous local high temperature and high pressure generated when the cavitation bubble collapses can accelerate the chemical reaction; in the liquid-liquid reaction system, the mechanical action and super-mixing effect of ultrasound can make the liquid-liquid phase mix, The formation of very fine emulsions increases the contact between phases and accelerates chemical reactions. These may be the reasons why ultrasound can accelerate the epoxidation of vegetable oils. Therefore the present invention just utilizes these unique effects of ultrasound, and utilizes ultrasonic conditions to prepare epoxy vegetable oil for the first time, which can simultaneously improve the epoxy value and epoxy conversion rate of epoxidized vegetable oil, and shorten the time of epoxidation reaction simultaneously Compared with the condition of not using ultrasonic, the epoxidation reaction time is shortened by 70% to 90%, which can reduce the operating cost, so that the present invention has better economy.

具体实施方式 Detailed ways

本发明以下将结合实施例作进一步详述:The present invention will be described in further detail below in conjunction with embodiment:

实施例1:Example 1:

a、取一定量的大豆油置于反应容器中,再将反应容器置于超声设备中;a. Take a certain amount of soybean oil and place it in a reaction vessel, and place the reaction vessel in an ultrasonic device;

b、取a步骤所取大豆油体积的15%的甲酸,以及a步骤所取大豆油体积的0.75%的催化剂(硫酸)进行搅拌混合,制备成混合液;B, get the formic acid of 15% of the volume of soybean oil taken in step a, and the catalyst (sulfuric acid) of 0.75% of the volume of soybean oil taken in step a, stir and mix, and prepare a mixed solution;

c、将b步骤所制备的混合液边搅拌边加入到a步骤的反应体系中;c, adding the mixed solution prepared in step b to the reaction system in step a while stirring;

d、调节c步骤所得体系的温度后开启超声装置,同时向其中缓慢滴加双氧水,控制超声的频率和功率;滴加双氧水时体系的温度为35℃,滴加的双氧水的质量百分比浓度为70%,体积为大豆油体积的35%,超声的频率为28kHz,超声功率为150w;d. After adjusting the temperature of the system obtained in step c, turn on the ultrasonic device, and slowly add hydrogen peroxide dropwise to it, and control the frequency and power of the ultrasonic wave; when adding hydrogen peroxide, the temperature of the system is 35°C, and the concentration of the dropped hydrogen peroxide is 70% by mass. %, the volume is 35% of the soybean oil volume, the ultrasonic frequency is 28kHz, and the ultrasonic power is 150w;

e、双氧水滴加完毕后,再次调节体系温度为50℃,并在超声频率为28kHz,超声功率为120w,时间为15min条件下进行环氧化反应;反应完成后,降至室温,静置后去除下层,得到粗环氧化植物油;e. After the addition of hydrogen peroxide is completed, adjust the temperature of the system to 50°C again, and carry out the epoxidation reaction under the conditions of ultrasonic frequency of 28kHz, ultrasonic power of 120w, and time of 15min; Remove the lower layer to obtain crude epoxidized vegetable oil;

f、将e步骤得到的粗环氧化植物油转移至水洗设备中,进行水洗,静置后去除水层;f, transfer the crude epoxidized vegetable oil obtained in step e to water washing equipment, wash with water, and remove the water layer after standing;

g、将f步骤得到的液体转移到减压蒸馏装置中,减压蒸馏脱除水分,得到环氧化豆油产品。环氧值为6.93%,环氧转化率为89.53%。g. Transfer the liquid obtained in step f to a vacuum distillation device, and remove moisture by vacuum distillation to obtain an epoxidized soybean oil product. The epoxy value is 6.93%, and the epoxy conversion rate is 89.53%.

实施例2:Example 2:

a、取一定量的大豆油置于反应容器中,再将反应容器置于超声设备中;a. Take a certain amount of soybean oil and place it in a reaction vessel, and place the reaction vessel in an ultrasonic device;

b、取a步骤所取大豆油体积的10%的冰乙酸,以及a步骤所取大豆油体积的0.95%的催化剂(硬脂酸)进行搅拌混合,制备成混合液;B, get the glacial acetic acid of 10% of the volume of soybean oil taken in step a, and the catalyst (stearic acid) of 0.95% of the volume of soybean oil taken in step a, stir and mix, and prepare a mixed solution;

c、将b步骤所制备的混合液边搅拌边加入到a步骤的反应体系中;c, adding the mixed solution prepared in step b to the reaction system in step a while stirring;

d、调节c步骤所得体系的温度后开启超声,同时向其中缓慢滴加双氧水,控制超声的频率和功率。滴加双氧水时体系的温度为45℃,滴加的双氧水的质量百分比浓度为30%,体积为大豆油体积的70%,超声的频率为45kHz,超声功率为180w;d. After adjusting the temperature of the system obtained in step c, turn on the ultrasonic wave, and slowly add hydrogen peroxide thereinto, and control the frequency and power of the ultrasonic wave. When hydrogen peroxide is added dropwise, the temperature of the system is 45°C, the mass percent concentration of the hydrogen peroxide added is 30%, the volume is 70% of the volume of soybean oil, the ultrasonic frequency is 45kHz, and the ultrasonic power is 180w;

e、双氧水滴加完毕后,再次调节体系温度为70℃,并在超声频率为100kHz,超声功率为210w,时间为30min条件下进行环氧化反应;反应完成后,降至室温,静置后去除下层,得到粗环氧化豆油;e. After the addition of hydrogen peroxide is completed, adjust the temperature of the system to 70°C again, and carry out the epoxidation reaction under the conditions of ultrasonic frequency of 100kHz, ultrasonic power of 210w, and time of 30min; Remove the lower layer to obtain crude epoxidized soybean oil;

f、将e步骤得到的粗环氧化豆油转移至水洗设备中,进行水洗,静置后去除水层;f, the crude epoxidized soybean oil obtained in step e is transferred to water washing equipment, washed with water, and the water layer is removed after standing;

g、将f步骤得到的液体转移到减压蒸馏装置中,减压蒸馏脱除水分,得到环氧化豆油产品。环氧值为7.26,环氧转化率为93.80%。g. Transfer the liquid obtained in step f to a vacuum distillation device, and remove moisture by vacuum distillation to obtain an epoxidized soybean oil product. The epoxy value is 7.26, and the epoxy conversion rate is 93.80%.

实施例3:Example 3:

a、取一定量的亚麻油置于反应容器中,再将反应容器置于超声设备中;a. Take a certain amount of linseed oil and place it in a reaction vessel, and then place the reaction vessel in an ultrasonic device;

b、取a步骤所取亚麻油体积的20%的甲酸,以及a步骤所取亚麻油体积的1.05%的催化剂(磷酸)进行搅拌混合,制备成混合液;B, get the formic acid of 20% of the volume of linseed oil taken in step a, and the catalyst (phosphoric acid) of 1.05% of the volume of linseed oil taken in step a, stir and mix, and prepare mixed solution;

c、将b步骤所制备的混合液边搅拌边加入到a步骤的反应体系中;c, adding the mixed solution prepared in step b to the reaction system in step a while stirring;

d、调节c步骤所得体系的温度后开启超声,同时向其中缓慢滴加双氧水,控制超声的频率和功率;滴加双氧水时体系的温度为55℃,滴加的双氧水的质量百分比浓度为80%,体积为亚麻油体积的30%,超声的频率为45kHz,超声功率为300w;d. Turn on the ultrasound after adjusting the temperature of the system obtained in step c, and slowly add hydrogen peroxide dropwise therein to control the frequency and power of the ultrasound; when adding hydrogen peroxide, the temperature of the system is 55°C, and the concentration of the hydrogen peroxide dropped is 80% by mass , the volume is 30% of the volume of linseed oil, the ultrasonic frequency is 45kHz, and the ultrasonic power is 300w;

e、双氧水滴加完毕后,再次调节体系温度为70℃,并在超声频率为28kHz,超声功率为210w,时间为65min条件下进行环氧化反应;反应完成后,降至室温,静置后去除下层,得到粗环氧化亚麻油;e. After the addition of hydrogen peroxide is completed, adjust the temperature of the system to 70°C again, and carry out the epoxidation reaction under the conditions of ultrasonic frequency of 28kHz, ultrasonic power of 210w, and time of 65min; The lower layer is removed to obtain crude epoxidized linseed oil;

f、将e步骤得到的粗环氧化亚麻油转移至水洗设备中,进行水洗,静置后去除水层;f, the thick epoxidized linseed oil obtained in e step is transferred to the water washing equipment, washed with water, and the water layer is removed after standing;

g、将f步骤得到的液体转移到减压蒸馏装置中,减压蒸馏脱除水分,得到环氧化亚麻油产品。环氧值为9.18%,环氧转化率为90.13%。g. The liquid obtained in step f is transferred to a vacuum distillation device, and moisture is removed by vacuum distillation to obtain an epoxidized linseed oil product. The epoxy value is 9.18%, and the epoxy conversion rate is 90.13%.

实施例4:Example 4:

a、取一定量的棉籽油置于反应容器中,再将反应容器置于超声设备中;a. Take a certain amount of cottonseed oil and place it in a reaction vessel, and place the reaction vessel in an ultrasonic device;

b、取a步骤所取棉籽油体积的25%的甲酸,以及a步骤所取棉籽油体积的0.80%的催化剂(磷酸)进行搅拌混合,制备成混合液;B, get the formic acid of 25% of the volume of cottonseed oil taken in step a, and the catalyst (phosphoric acid) of 0.80% of the volume of cottonseed oil taken in step a, stir and mix, and prepare a mixed solution;

c、将b步骤所制备的混合液边搅拌边加入到a步骤的反应体系中;c, adding the mixed solution prepared in step b to the reaction system in step a while stirring;

d、调节c步骤所得体系的温度后开启超声,同时向其中缓慢滴加双氧水,控制超声的频率和功率。滴加双氧水时体系的温度为60℃,滴加的双氧水的质量百分比浓度为50%,体积为棉籽油体积的40%,超声的频率为28kHz,超声功率为240w;d. After adjusting the temperature of the system obtained in step c, turn on the ultrasonic wave, and slowly add hydrogen peroxide thereinto, and control the frequency and power of the ultrasonic wave. When the hydrogen peroxide is added dropwise, the temperature of the system is 60°C, the concentration of the hydrogen peroxide dropped is 50% by mass, the volume is 40% of the volume of cottonseed oil, the ultrasonic frequency is 28kHz, and the ultrasonic power is 240w;

e、双氧水滴加完毕后,再次调节体系温度为50℃,并在超声频率为45kHz,超声功率为180w,时间为75min条件下进行环氧化反应;反应完成后,降至室温,静置后去除下层,得到粗环氧化棉籽油;e. After the addition of hydrogen peroxide is completed, adjust the temperature of the system to 50°C again, and carry out the epoxidation reaction under the conditions of ultrasonic frequency of 45kHz, ultrasonic power of 180w, and time of 75min; The lower layer is removed to obtain crude epoxidized cottonseed oil;

f、将e步骤得到的粗环氧化棉籽油转移至水洗设备中,进行水洗,静置后去除水层;f, transfer the thick epoxidized cottonseed oil that step e obtains to washing equipment, wash with water, and remove the water layer after standing;

g、将f步骤得到的液体转移到减压蒸馏装置中,减压蒸馏脱除水分,得到环氧化棉籽油产品。环氧值为5.61%,环氧转化率为87.26%。g. Transfer the liquid obtained in step f to a vacuum distillation device, and remove moisture by vacuum distillation to obtain an epoxidized cottonseed oil product. The epoxy value is 5.61%, and the epoxy conversion rate is 87.26%.

Claims (4)

1、一种超声条件下环氧化油脂的制备方法,其特征在于所述方法包括以下步骤:1, a preparation method of epoxidized grease under ultrasonic conditions, it is characterized in that described method comprises the following steps: a、取一定量的植物油置于反应容器中,再将反应容器置于超声设备中;a. Take a certain amount of vegetable oil and place it in a reaction vessel, and then place the reaction vessel in an ultrasonic device; b、取a步骤所取植物油体积的10%~25%的甲酸、冰乙酸或甲酸与冰乙酸的混合物,以及a步骤所取植物油体积的0.75%~1.05%的催化剂进行搅拌混合,制备成混合液;B, take 10%~25% formic acid, glacial acetic acid or the mixture of formic acid and glacial acetic acid of the volume of vegetable oil taken in step a, and the catalyst of 0.75%~1.05% of the volume of vegetable oil taken in step a, stir and mix, and prepare the mixture liquid; c、将b步骤所制备的混合液边搅拌边加入到a步骤的反应容器中;c, adding the mixed solution prepared in step b into the reaction vessel of step a while stirring; d、调节体系的温度后开启超声设备,同时开始向c步骤所得体系中缓慢滴加双氧水,控制超声的频率和功率;滴加双氧水时体系的温度为35℃~60℃,滴加的双氧水体积为所取植物油体积的30%~70%,超声的频率为28kHz~100kHz,超声功率为120w~300w;d. After adjusting the temperature of the system, turn on the ultrasonic equipment, and at the same time start to slowly add hydrogen peroxide to the system obtained in step c, and control the frequency and power of the ultrasonic; 30% to 70% of the volume of the vegetable oil taken, the frequency of ultrasound is 28kHz to 100kHz, and the power of ultrasound is 120w to 300w; e、双氧水滴加完毕后,再次调节体系温度至50℃~75℃,并在超声频率为28kHz~100kHz,超声功率为120w~300w,时间为15min~75min条件下进行环氧化反应;反应完成后,降至室温,静置后去除下层,得到粗环氧化植物油;e. After the addition of hydrogen peroxide is completed, adjust the temperature of the system again to 50°C-75°C, and carry out the epoxidation reaction under the conditions of ultrasonic frequency of 28kHz-100kHz, ultrasonic power of 120w-300w, and time of 15min-75min; the reaction is completed Afterwards, be down to room temperature, remove lower layer after leaving standstill, obtain crude epoxidized vegetable oil; f、将e步骤得到的粗环氧化植物油转移至水洗设备中,进行水洗,静置后去除水层;f, transfer the crude epoxidized vegetable oil obtained in step e to water washing equipment, wash with water, and remove the water layer after standing; g、将f步骤得到的液体转移到减压蒸馏装置中,减压蒸馏脱除水分,得到环氧化植物油产品。g. Transfer the liquid obtained in step f to a vacuum distillation device, and remove moisture by vacuum distillation to obtain an epoxidized vegetable oil product. 2、根据权利要求1所述的在超声条件下环氧化油脂的制备方法,其特征在于:所述催化剂为硫酸、磷酸、硬脂酸、油酸、硫酸铝、氯磺酸、酒石酸、杂多酸中的一种或一种以上。2. The method for preparing epoxidized grease under ultrasonic conditions according to claim 1, characterized in that: the catalyst is sulfuric acid, phosphoric acid, stearic acid, oleic acid, aluminum sulfate, chlorosulfonic acid, tartaric acid, miscellaneous One or more of the polyacids. 3、根据权利要求1所述的在超声条件下环氧化油脂的制备方法,其特征在于:所述的植物油是大豆油、红花油、向日葵油、亚麻油、蓖麻油、菜籽油、桐油、棕榈油、花生油、脱水蓖麻油中的一种或一种以上混合物。3. The method for preparing epoxidized oil under ultrasonic conditions according to claim 1, wherein said vegetable oil is soybean oil, safflower oil, sunflower oil, linseed oil, castor oil, rapeseed oil, One or more mixtures of tung oil, palm oil, peanut oil, dehydrated castor oil. 4、根据权利要求1所述的在超声条件下环氧化油脂的制备方法,其特征在于:所述的双氧水的质量百分比浓度为30%~80%。4. The method for preparing epoxidized grease under ultrasonic conditions according to claim 1, characterized in that: the mass percent concentration of the hydrogen peroxide is 30%-80%.
CN200910065464XA 2009-07-20 2009-07-20 Method for preparing epoxidized oil under ultrasound condition Expired - Fee Related CN101613639B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN200910065464XA CN101613639B (en) 2009-07-20 2009-07-20 Method for preparing epoxidized oil under ultrasound condition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN200910065464XA CN101613639B (en) 2009-07-20 2009-07-20 Method for preparing epoxidized oil under ultrasound condition

Publications (2)

Publication Number Publication Date
CN101613639A true CN101613639A (en) 2009-12-30
CN101613639B CN101613639B (en) 2012-01-04

Family

ID=41493530

Family Applications (1)

Application Number Title Priority Date Filing Date
CN200910065464XA Expired - Fee Related CN101613639B (en) 2009-07-20 2009-07-20 Method for preparing epoxidized oil under ultrasound condition

Country Status (1)

Country Link
CN (1) CN101613639B (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101942043A (en) * 2010-09-25 2011-01-12 中国热带农业科学院农产品加工研究所 Method for preparing epoxidized natural rubber
CN102199480A (en) * 2010-03-24 2011-09-28 河南工业大学 Method for preparing lubricating agent by utilizing palm liquid oil
CN102703224A (en) * 2012-06-06 2012-10-03 北京林氏精化新材料有限公司 Method for preparing substance containing epoxyfatty acid low carbon alcohol ester plasticizer by palm oil
CN103382415A (en) * 2013-01-14 2013-11-06 江苏卡特新能源有限公司 Production method of epoxidized fatty acid methyl ester/epoxidized soybean oil
CN103725348A (en) * 2013-12-18 2014-04-16 张家港市林达外加剂厂 Method for preparing lubricating oil base oil

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102199480A (en) * 2010-03-24 2011-09-28 河南工业大学 Method for preparing lubricating agent by utilizing palm liquid oil
CN102199480B (en) * 2010-03-24 2013-05-01 河南工业大学 Method for preparing lubricating agent by utilizing palm liquid oil
CN101942043A (en) * 2010-09-25 2011-01-12 中国热带农业科学院农产品加工研究所 Method for preparing epoxidized natural rubber
CN102703224A (en) * 2012-06-06 2012-10-03 北京林氏精化新材料有限公司 Method for preparing substance containing epoxyfatty acid low carbon alcohol ester plasticizer by palm oil
CN103382415A (en) * 2013-01-14 2013-11-06 江苏卡特新能源有限公司 Production method of epoxidized fatty acid methyl ester/epoxidized soybean oil
CN103382415B (en) * 2013-01-14 2014-09-03 江苏卡特新能源有限公司 Production method of epoxidized fatty acid methyl ester/epoxidized soybean oil
CN103725348A (en) * 2013-12-18 2014-04-16 张家港市林达外加剂厂 Method for preparing lubricating oil base oil

Also Published As

Publication number Publication date
CN101613639B (en) 2012-01-04

Similar Documents

Publication Publication Date Title
CN103601703B (en) The method of epoxidation methyl eleostearate is prepared by tung oil
CN101613639A (en) Preparation method of epoxidized oil under ultrasonic condition
US9546143B2 (en) Method for preparing high-quality epoxidized fatty acid ester with micro-reaction device
CN102876462B (en) A method for preparing high-quality epoxidized soybean oil
CN103013682B (en) Synthetic method for epoxy soybean oil acrylate
CN104262297B (en) Method for preparing high-quality epoxy vegetable oil by adopting microreactor
CN101591588A (en) Organic rhenium oxide-carbamide peroxide catalyzes the method for preparing epoxy soybean oil or epoxy fatty acid methyl (ethyl) ester
CN102993133A (en) Method for preparing epoxy fatty acid methyl ester by one-step method through microreactor
CN1667106A (en) Vegetable oil with high epoxy value and its preparation method and application
CN103224837B (en) Rapid and green preparation method of epoxidation soybean oil
CN104292187B (en) Method for preparing high-quality epoxidized soybean oil
CN108070093B (en) Preparation method of water-based epoxy resin emulsion
CN108456277A (en) A kind of molecular imprinted polymer on surface material of redox graphene
CN108384043A (en) A kind of molecular imprinted polymer on surface material
CN102367280B (en) Preparation method of starch octenyl succiniade under supercritical condition
CN102060812A (en) Method for preparing epoxy fatty acid methyl ester
CN104086513A (en) Method for preparing epoxy soybean oil by utilizing high-concentration oxydol reaction heat
CN104744703B (en) Silicon-containing tung oil-based alkyd resin as well as preparation method and application of alkyd resin
CN104693418B (en) A kind of epoxy resin cure film of high fat content and its preparation method and application
CN105801520A (en) Method for preparing epoxy fatty acid ester by using micro-reaction device
CN104356328B (en) Preparation method of soybean oil rosin combined chemical modified phenolic resin and modified phenolic resin
CN102489333A (en) Composite catalyst for epoxidation of fatty acid methyl ester
CN106220903A (en) A kind of preparation method of graphene oxide/sodium alginate composite
CN110204514A (en) A kind of production technology of epoxidized vegetable oil
CN101186597A (en) Method for preparing epoxy soybean acidified oil (C1-4) without protonic acid

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120104

Termination date: 20120720