Heteropoly acid catalyst and preparation method thereof

A technology of catalyst and heteropolyacid, which is applied in the field of supported heteropolyacid catalyst and its preparation, can solve the problems of high reaction temperature requirements, achieve high anti-coking performance, increase total acid content, high activity and selectivity Effect

Active Publication Date: 2016-06-29
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Using ethanol aqueous solution with a concentration of 5-100% as raw material, the catalyst exhibits high ethanol conversion and e

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0020] Example 1

[0021] (1) Preparation of the carrier:

[0022] Add 2.9g of citric acid and 3.0g of polyethylene glycol 200 to deionized water to form a mixed solution, then add 33.2mL of ethyl orthosilicate, stir evenly, and add to the prepared 79.2g particle size of 0.1mm. In spherical alumina, stirred at 60 °C for 2 h, then stirred at 80 °C until gelatinized, aged at 40 °C for 8 h, then dried at 110 °C for 8 h, and calcined at 550 °C for 3 h to obtain silica-coated alumina Alumina carrier, wherein silicon oxide accounts for 10% of the weight of the carrier, the molar ratio of citric acid to silicon oxide is 0.1, and the molar ratio of polyethylene glycol 200 to silicon oxide is 0.1.

[0023] (2) Preparation of catalyst: The catalyst is prepared by supersaturation impregnation method, and the steps are as follows:

[0024] 7.1 g of boric acid and 8.3 g of phosphotungstic acid were added to deionized water to prepare a mixed solution; the prepared carrier was added to th...

Example Embodiment

[0029] Example 2

[0030] (1) Preparation of the carrier:

[0031] Add 4.8g of citric acid and 15.0g of polyethylene glycol 600 into deionized water to form a mixed solution, then add 37.8mL of ethyl orthosilicate, stir evenly, and add to the prepared 73.0g particle size of 0.5mm. In spherical alumina, stir at 60°C for 2h, then stir at 80°C until gelling, age at 40°C for 8h, then dry at 110°C for 8h, and calcinate at 550°C for 3h to obtain silica coating The alumina carrier, wherein silicon oxide accounts for 12% of the weight of the carrier, the molar ratio of citric acid to silicon oxide is 0.15, and the molar ratio of polyethylene glycol 600 to silicon oxide is 0.15.

[0032] (2) Preparation of catalyst: The catalyst is prepared by supersaturation impregnation method, and the steps are as follows:

[0033] 8.9 g of boric acid and 12.5 g of phosphotungstic acid were added to deionized water to prepare a mixed solution; the prepared carrier was added to the mixed solution, ...

Example Embodiment

[0036] Example 3

[0037] (1) Preparation of the carrier:

[0038] Add 7.6g of citric acid and 14.3g of polyethylene glycol 400 to deionized water to form a mixed solution, then add 44.9mL of ethyl orthosilicate, stir evenly, and add to the prepared 67.2g particle size of 0.3mm. In spherical alumina, stirred at 60 °C for 2 h, then stirred at 80 °C until gelatinized, aged at 40 °C for 8 h, then dried at 110 °C for 8 h, and calcined at 550 °C for 3 h to obtain silica-coated alumina Alumina carrier, wherein silicon oxide accounts for 15% of the weight of the carrier, the molar ratio of citric acid to silicon oxide is 0.2, and the molar ratio of polyethylene glycol 400 to silicon oxide is 0.18.

[0039] (2) Preparation of catalyst: The catalyst is prepared by supersaturation impregnation method, and the steps are as follows:

[0040] Add 10.6 g of boric acid and 15.6 g of phosphotungstic acid to deionized water to prepare a mixed solution; add the prepared carrier to the mixed s...

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PUM

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Abstract

The invention discloses a heteropoly acid catalyst and a preparation method thereof. The catalyst adopts alumina as the carrier, uses heteropoly acid as the active component, and takes boron oxide as the assistant, wherein the surface of the alumina carrier is coated with silica. The preparation method consists of: coating the surface of the alumina carrier with an appropriate amount of silica, and then loading heteropoly acid and the assistant component. The catalyst has high activity and selectivity when used for preparation of ethylene by ethanol dehydration.

Description

technical field [0001] The invention relates to a heteropolyacid catalyst and a preparation method thereof, in particular to a supported heteropolyacid catalyst for ethanol dehydration to ethylene and a preparation method thereof. Background technique [0002] Ethylene is a basic organic chemical raw material and a leading product in the petrochemical industry. About 75% of chemical products are prepared from ethylene. Therefore, ethylene production has become an important indicator to measure the development level of a country's petrochemical industry. Traditional ethylene is mainly produced through the distillation and cracking of light petroleum, which relies heavily on petroleum resources. With the increasingly tense international energy situation and the depletion of oil resources, it is imperative to develop new renewable alternative energy sources. [0003] Recently, the dehydration of ethanol, especially renewable bioethanol, to ethylene has attracted more and more ...

Claims

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Application Information

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IPC IPC(8): B01J31/26C07C11/04C07C1/24
CPCY02P20/52
Inventor 金浩孙素华朱慧红刘杰杨光蒋立敬
Owner CHINA PETROLEUM & CHEM CORP
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