Process for producing alkylidene dibasic alcohol
A technology for alkylene glycol and alkylene oxide, which is applied in the field of preparing alkylene glycol by catalytic hydration of alkylene oxide, can solve the problems of short service life of catalyst, poor heat resistance, etc. The effect of good thermal stability, selectivity and yield improvement
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[0039] Preparation method of composite resin
[0040] 【Example】
[0041] In a 250 ml three-neck bottle, add 120 ml of distilled water and 0.6 g of polyvinyl alcohol, start stirring and raise the temperature to completely dissolve the polyvinyl alcohol. Stop stirring, add the monomer mixture solution containing initiator (20.4 grams of styrene, 6.1 grams of divinylbenzene, 3.9 grams of carbon nanotubes, 1.4 grams of benzoyl peroxide) after cooling down slightly, start stirring, and heat up to 85 ° C. React for 5 hours. The temperature was raised to 95°C for about 2 hours. After the reaction, pour out the upper liquid, wash with 85°C hot water for several times, and then wash with cold water for several times, then filter, dry, and weigh to obtain composite beads. Functionalization of composite beads: Add 20.6 grams of composite beads A and 80 milliliters of chloromethyl ether into a 500-ml three-necked bottle, start stirring and heat up to 30°C, add 8 grams of zinc chloride ...
Embodiment 1~5
[0054] 15 milliliters of each of the above-mentioned catalysts A, B, C, D, and E (grain size 20-40 mesh) were packed in a stainless steel fixed-bed reactor with a diameter of 10 mm and a length of 350 mm respectively, and the raw material water and ethylene oxide Alkanes are fed with a metering pump at a molar ratio of 12:1. The pressure of the reaction system is 1.2 MPa, the reaction temperature is 90°C, and the liquid space velocity is 3 hours -1 , The product was qualitatively and quantitatively analyzed by HP5890 gas chromatography, and the results are listed in Table 1.
Embodiment 6
[0058] 15 milliliters of the above-mentioned catalyst C (particle size 20-40 mesh) is packed in a stainless steel fixed-bed reactor with a diameter of 10 mm and a length of 350 mm, and feed water and ethylene oxide with a metering pump at a molar ratio of 22:1. material. The pressure of the reaction system is 1.2 MPa, the reaction temperature is 90°C, and the liquid space velocity is 6 hours -1 , The product was qualitatively and quantitatively analyzed by HP5890 gas chromatography, and the results are listed in Table 1.
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