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Catalyst for ethoxylation and use thereof

An ethoxylation and catalyst technology, which is applied in the field of catalysts for ethoxylation synthesis reactions, can solve the problems of slow reaction speed and large amount of catalyst, and achieve fast reaction speed, high conversion rate of methyl ester, and high product yield Effect

Inactive Publication Date: 2003-10-29
中轻日化科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] Although the catalysts of these two companies can effectively complete the ethoxylation reaction of raw materials without active hydrogen in the terminal group, the amount of catalyst used is relatively large and must be filtered out from the product. The reaction speed is relatively slow, and the average addition rate is about 1gEO / g cat min

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] Mix 68.4g of MgO and 28g of diatomaceous earth evenly, add to 400ml of aqueous solution containing 23g of aluminum chloride, stir for 1hr, wash, dry, calcinate at 500°C for 1hr, grind, and sieve to obtain a Mg-Al composite catalyst . The catalyst powder contains 65% of magnesium oxide, 8.4% of aluminum oxide and 26.6% of diatomite.

[0037] Above-mentioned catalyzer 1.0g is joined in the 154g coconut oil methyl ester, drops in the 1L autoclave while stirring, N 2 Replace three times, raise the temperature to 130°C, introduce ethylene oxide (EO), keep the reaction temperature at 170°C, 0.3MPa, react for about 26min until the amount of EO added is 277g, age for 10min, cool to 70°C, release the material, weigh 431g , to obtain a product with an average oxyethylene content of 9.0—coco methyl ester ethoxylate.

Embodiment 2

[0039] Add 300ml of an aqueous solution containing 85g of aluminum nitrate and 27g of diatomaceous earth dropwise into 150ml of a dispersion containing 58g of CaO, and stir for 1 hr at room temperature to obtain a mixed catalyst slurry, which is removed by a strongly basic anion exchange resin. NO - 3 After the ion exchange is completed, the catalyst is separated from the ion resin, dried, calcined at 500° C. for 1 hr, ground and sieved to obtain a Ca-Al composite catalyst. The catalyst powder contains 60% of calcium oxide, 12% of aluminum oxide and 28% of diatomite.

[0040] With above-mentioned catalyzer 1.8g, add 182g methyl laurate, drop into 1L autoclave while stirring, N 2 Replaced three times, heated to 140°C, introduced EO, and kept the reaction temperature at 175°C, 0.4MPa, reacted for about 18 minutes until the amount of EO added was 300g, aged for 10 minutes, cooled to 70°C, released the material, weighed 483g, and obtained the average ethylene oxide The product ...

Embodiment 3

[0042] Mix 20g of MgO powder with 9g of 4A zeolite, add to 500ml of aqueous solution containing 1.9% gallium nitrate, stir vigorously for 1hr, dry at 110°C for 2hr, calcined at 500°C for 1hr, grind and sieve to obtain a gallium ion-containing MgO composite catalyst. The catalyst powder contains 61.6% of magnesium oxide, 10.7% of gallium oxide and 27.7% of 4A zeolite.

[0043] Above-mentioned catalyzer 3.5g is joined in the 220g coconut oil methyl ester, drops in the 1L autoclave while stirring, N 2 Replace three times, heat up to 130°C, introduce ethylene oxide (EO), keep the reaction temperature at 165°C, 0.3MPa, react for about 13 minutes until the amount of EO added is 352g, age for 10 minutes, cool to 70°C, release the material, weigh 574.5 g, obtain the product---coco methyl ester ethoxylate that average oxyethylene group content is 8.0.

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PUM

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Abstract

A catalyst for the ethoxylation of feedstock without reactive hydrogen in its terminal group with epoxy ethane contains the oxide of alkali-earth metal (30-90 wt.%), the ions of group III metal (1-40wt.%), and carrier (1-30 wt.%). Its advantages are less consumption of catalyst, high reaction speed, high conversion of methylester, and high yield of product.

Description

[0001] Field: [0002] The invention belongs to a catalyst used for the synthesis reaction of ethoxylation of terminal group-free active hydrogen raw materials and its application. Background technique: [0003] Generally speaking, the nonionic surfactants derived from ethylene oxide have an active or unstable hydrogen atom in their hydrophobic raw materials, and this hydrogen atom is connected to a heteroatom such as O or N. Catalysts such as NaOH, KOH or NaOCH 3 Under the action of etc., the active hydrogen is easily removed to form an active anion with the base, which then quickly reacts with ethylene oxide (EO) to form an ethoxylate. However, for raw materials without active end groups such as fatty acid methyl ester, under the action of the above-mentioned basic catalyst, the conversion rate of methyl ester is very low, generally <50%, and the product oxyethylene group has a wide distribution. [0004] In 1990, Vista Chemical Company (now CONDEA Vista Company) develo...

Claims

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Application Information

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IPC IPC(8): B01J23/02B01J23/08C07C41/00
Inventor 孙永强罗毅张高勇田春花刘广宇张威
Owner 中轻日化科技有限公司
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