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Catalysts for the production of monoethanolamine and diethanolamine

A technology of diethanolamine and a catalyst is applied in the field of catalysts for increasing the production of monoethanolamine and diethanolamine, and can solve the problems of stimulating the increase of monoethanolamine and diethanolamine output, increasing separation and production costs, and achieving the effect of good technical effect.

Active Publication Date: 2021-10-01
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] In recent years, the market demand for ethylenediamine, piperazine, triethylenediamine and other products has increased sharply, which has obviously stimulated the increase in the output of upstream products monoethanolamine and diethanolamine. The existing process co-produces triethanolamine and separates three Ethanolamine and its conversion to monoethanolamine and diethanolamine would increase separation and production costs significantly

Method used

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  • Catalysts for the production of monoethanolamine and diethanolamine

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0060] 1. Molecular sieve preparation

[0061] a) NaOH is first dissolved in water to obtain solution I, and NaAlO 2 Add to solution I to obtain solution II, add TBABr to solution II to obtain solution III, and finally add 40% silica sol, NaCl, polyethylene glycol (10000) to solution III to obtain a raw material mixture, each raw material in the compound The molar ratio is: SiO 2 / Al 2 o 3 =50,H 2 O / SiO 2 =50, NaCl / SiO 2 =0.68, NaOH / SiO 2 =0.15, TBABr / SiO 2 =0.40, polyethylene glycol (10000) / SiO 2 = 0.02. b) Stir the raw material mixture prepared in step a) for 180 minutes, put it into a reaction kettle, and perform dynamic (200 rpm) crystallization at 170° C. for 72 hours. The crystallized product was quenched, filtered, washed with water until the pH value was 7, and dried at 120°C for 12 hours to obtain the original powder of ZSM-11 molecular sieve

[0062] The prepared ZSM-11 molecular sieve powder was mixed with 0.2mol L -1 Soak in ammonium nitrate solution wi...

Embodiment 2

[0073] 1. Molecular sieve preparation

[0074] a) NaOH is first dissolved in water to obtain solution I, and NaAlO 2 Add to solution I to obtain solution II, add TBABr to solution II to obtain solution III, and finally add 40% silica sol, NaCl, polyethylene glycol (10000) to solution III to obtain a raw material mixture, each raw material in the compound The molar ratio is: SiO 2 / Al 2 o 3 =50,H 2 O / SiO 2 =50, NaCl / SiO 2 =0.68, NaOH / SiO 2 =0.15, TBABr / SiO 2 =0.40, polyethylene glycol (10000) / SiO 2 = 0.02. b) Stir the raw material mixture prepared in step a) for 180 minutes, put it into a reaction kettle, and perform dynamic (200 rpm) crystallization at 170° C. for 72 hours. The crystallized product was quenched, filtered, washed with water until the pH value was 7, and dried at 120°C for 12 hours to obtain the original powder of ZSM-11 molecular sieve

[0075] The prepared ZSM-11 molecular sieve powder was mixed with 0.2mol L -1 Soak in ammonium nitrate solution wi...

Embodiment 3

[0086] 1. Molecular sieve preparation

[0087] a) NaOH is first dissolved in water to obtain solution I, and NaAlO 2 Add to solution I to obtain solution II, add TBABr to solution II to obtain solution III, and finally add 40% silica sol, NaCl, polyethylene glycol (10000) to solution III to obtain a raw material mixture, each raw material in the compound The molar ratio is: SiO 2 / Al 2 o 3 =50,H 2 O / SiO 2 =50, NaCl / SiO 2 =0.68, NaOH / SiO 2 =0.15, TBABr / SiO 2 =0.40, polyethylene glycol (10000) / SiO 2 = 0.02. b) Stir the raw material mixture prepared in step a) for 180 minutes, put it into a reaction kettle, and perform dynamic (200 rpm) crystallization at 170° C. for 72 hours. The crystallized product was quenched, filtered, washed with water until the pH value was 7, and dried at 120°C for 12 hours to obtain the original powder of ZSM-11 molecular sieve

[0088] The prepared ZSM-11 molecular sieve powder was mixed with 0.2mol L -1 Soak in ammonium nitrate solution wi...

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Abstract

The present invention relates to a catalyst for increasing the production of monoethanolamine and diethanolamine, which mainly solves the problems of by-product triethanolamine (TEA) and high energy consumption for product separation in the production of monoethanolamine (MEA) and diethanolamine (DEA) in the prior art, and provides a A kind of catalyst that is used to increase production monoethanolamine and diethanolamine, by adopting the catalyst that is used to increase production monoethanolamine and diethanolamine, comprises ZSM‑11 molecular sieve, and molecular sieve modification element, and described modification element comprises the technical scheme of La and Ni This problem is well solved and can be used in the industrial production of monoethanolamine and diethanolamine.

Description

technical field [0001] The present invention relates to catalysts for increasing the production of monoethanolamine and diethanolamine. Background technique [0002] Ethanolamine (EA) is the general term for the products in which the hydrogen atoms in the ammonia molecule are replaced by one, two or three hydroxyethanols, respectively called monoethanolamine (MEA), diethanolamine (DEA) and triethanolamine (TEA). The ethanolamine compound contains two functional groups: hydroxyl group and amine group, so it has some chemical properties and new properties of alcohol and amine compounds. The characteristics and interactions of the two functional groups make it an important organic intermediate and chemical end product with a wide range of uses. One of the uses of ethanolamine is to synthesize important basic raw materials for surfactants, medicines, polyurethane additives, rubber processing additives, antifreeze additives and other products. [0003] At present, foreign compa...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/46C07C213/02C07C215/08C07C215/12
CPCB01J29/46B01J2229/18C07C213/02C07C215/08C07C215/12
Inventor 刘师前钱斌刘仲能韩亚梅
Owner CHINA PETROLEUM & CHEM CORP