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Catalyst and method for preparing glycine methyl ester and glycine through catalytic amination of methyl glycolate

A catalyst, glycine technology, applied in the direction of metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, molecular sieve catalyst, etc., can solve problems such as cost increase, achieve low cost, improve activity and stability, Inexpensive effect

Inactive Publication Date: 2021-07-13
上海卓笙环保科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] For this reason, the embodiment of the present invention provides a catalyst and method for producing glycine methyl ester and glycine by catalytic amination of methyl glycolate. The catalyst is prepared by a carrier and an active component, which can catalyze methyl glycolate and ammonia or ammonia gas / One-step reaction of water vapor to prepare glycine methyl ester and / or glycine with high activity and high selectivity, without the use of noble metals, and the ratio of reaction products can be adjusted as needed to solve the problem of increased cost due to the addition of platinum group metals in the prior art

Method used

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  • Catalyst and method for preparing glycine methyl ester and glycine through catalytic amination of methyl glycolate
  • Catalyst and method for preparing glycine methyl ester and glycine through catalytic amination of methyl glycolate

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Embodiment 1

[0027] This example is used to illustrate the catalyst of the present invention, its preparation method and the method for preparing glycine methyl ester by catalytic amination of methyl glycolate.

[0028] (1) Preparation of a composite silica carrier containing Beta zeolite: Add Ludox silica sol and Beta zeolite into the reaction tank. The specific reaction conditions include: the initial reaction temperature is 25°C, and the initial concentration of silica sol is 20g SiO 2 ·L -1 , after stirring and aging at 25°C for 2h, the resulting solution was evaporated to dryness, dried at 120°C for 14h, kneaded and then calcined at 600°C for 5h to prepare a composite silica carrier with a Beta zeolite content of 10wt% based on the weight of the carrier .

[0029] (2) Co(NO 3 ) 2 , Ni(NO 3 ) 2 , Cu(NO 3 ) 2 , Fe(NO 3 ) 3 and Zn(NO 3 ) 2 Prepare a solution and impregnate the carrier obtained in step (1), dry at 120°C for 2h, and roast at 380°C for 4h to prepare a catalyst wi...

Embodiment 2

[0032] This example is used to illustrate the catalyst of the present invention, its preparation method and the method for preparing glycine by direct catalytic amination of methyl glycolate.

[0033] (1) Preparation of composite alumina carrier containing ZSM-5 zeolite: Add ZSM-5 zeolite and 200ml water into the reaction kettle, use nitric acid to adjust the pH value of the reaction system to 5.0, and then add nitric acid and sodium metaaluminate in parallel In the reaction kettle, the reaction conditions include: the temperature is 40°C, the mass concentration of sodium metaaluminate is 100g / L, the gelation time is 1.2h, the end point pH value is 7.0, keep the temperature unchanged for 2h, and then wash to remove impurities , dried at 120° C. for 20 hours, kneaded and then calcined at 550° C. for 4 hours to prepare a composite alumina carrier with a ZSM-5 zeolite content of 5 wt % based on the weight of the carrier.

[0034] (2) Co(NO 3 ) 2 , Ni(NO 3 ) 2 , Cu(NO 3 ) 2 ...

Embodiment 3

[0037] This example is used to illustrate the catalyst of the present invention, its preparation method and the method for preparing glycine methyl ester by catalytic amination of methyl glycolate.

[0038] (1) Preparation of a composite silica carrier containing mordenite and carbon black: Add Ludox silica sol, mordenite and carbon black to the reaction tank. The specific reaction conditions include: the initial reaction temperature is 20°C, and the initial concentration of silica sol is 30g SiO 2 ·L -1 , after stirring and aging at 25°C for 3h, the resulting solution was evaporated to dryness, dried at 120°C for 14h, kneaded and then calcined at 450°C for 4h to prepare a mordenite zeolite content of 7.5wt% and carbon black based on the weight of the carrier. Composite silica support with a content of 2.5 wt%.

[0039] (2) Co(NO 3 ) 2 , Ni(NO 3 ) 2 , Cu(NO 3 ) 2 , Fe(NO 3 ) 2 and Zn(NO 3 ) 2 Prepare a solution and impregnate the carrier obtained in step (1), dry at...

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Abstract

The invention discloses a catalyst and method for preparing glycine methyl ester and glycine through catalytic amination of methyl glycolate, and particularly relates to the field of fine chemical engineering. The catalyst comprises active components and a carrier, and is characterized in that the used active components (in percentage by weight) comprise 10-35 wt% of VIII group metal, 5-10 wt% of IB group metal and 8-25 wt% of IIB group metal, and the carrier comprises a water-resistant inorganic oxide, a molecular sieve and carbon. The catalyst is prepared through the carrier and the active components, the one-step reaction of methyl glycolate and ammonia gas or ammonia gas / water vapor can be catalyzed to prepare glycine methyl ester and / or glycine in a high-activity and high-selectivity mode, precious metal does not need to be used, and the proportion of reaction products can be adjusted according to needs.

Description

technical field [0001] The embodiment of the present invention relates to the field of fine chemical industry, in particular to a catalyst and a method for preparing glycine methyl ester and glycine by catalytic amination of methyl glycolate. Background technique [0002] Glycine, also known as aminoacetic acid, is the amino acid with the simplest structure. As an important fine chemical intermediate, it is widely used in the fields of pesticide, medicine, food, feed, daily chemical and electroplating. my country is the largest producer and consumer of glycine in the world, and the market size of glycine exceeds 350,000 tons. At present, the industrial production technologies of glycine mainly include the improved Streck method, the direct Hyne method and the ammonolysis method of chloroacetic acid. Due to the monopoly of foreign technology, the production of glycine in my country still uses the backward chloroacetic acid method. Compared with the improved Streck method and...

Claims

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Application Information

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IPC IPC(8): B01J29/76B01J29/46B01J29/24B01J29/14B01J23/80B01J37/02B01J37/08C07C227/08C07C227/18C07C229/08
CPCB01J29/7615B01J29/46B01J29/24B01J29/146B01J23/80B01J23/002B01J37/0201B01J37/088C07C227/08C07C227/18B01J2523/00
Inventor 席秋波王维君
Owner 上海卓笙环保科技有限公司