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Supported heteropolyacid catalyst and preparation method thereof

A technology of heteropolyacid and catalyst, applied in the field of supported heteropolyacid catalyst and its preparation, can solve the problems of poor low temperature activity, high equipment requirements and high reaction temperature

Active Publication Date: 2020-07-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] At present, the catalyst used for methanol dehydration is generally Al 2 o 3 Or molecular sieves, wherein commonly used molecular sieves include aluminum phosphate, HZSM-5, HY, SAPO, etc., and they all have their own advantages and disadvantages: although alumina has high stability, the reaction temperature is high, and the requirements for reaction equipment are very high, resulting in The cost is high; molecular sieve catalysts have strong acidity and low initial temperature, but they also have the disadvantages of many by-products, easy carbon deposition, and easy deactivation
When the above-mentioned catalyst is used to process pure methanol raw materials under normal pressure, its selectivity is relatively high, but its low-temperature activity is not good, and further improvement is needed.

Method used

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  • Supported heteropolyacid catalyst and preparation method thereof
  • Supported heteropolyacid catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] (1) Catalyst preparation

[0042] Weigh 600g of ammonium phosphate, dissolve it in 2000mL of deionized water to obtain solution A; grind 1000g of petroleum coke to powder, then add it to solution A, let it stand for 1.5h, then filter, and put the obtained solid sample in an oven at 110°C Dry for 5h. At 200°C, pretreat the dried solid sample with water vapor for 3 hours (the volumetric space velocity of the water vapor gas is 1200 hours -1 ), then raise the temperature to 400°C, continue pretreatment for 3h, and then cool to 60°C under nitrogen protection to obtain pretreated petroleum coke.

[0043] Mix 1000g of the pretreated petroleum coke obtained above, 38.5g of lanthanum nitrate and 2000g of potassium hydroxide evenly, place in a microwave heating furnace with a microwave frequency of 2450MHz, vacuumize, and heat up to 500 under the condition that the microwave power is 0.3kw ℃, keep it constant for 40min, then pass nitrogen gas to normal pressure, and continue t...

Embodiment 2

[0049] (1) Catalyst preparation

[0050] Weigh 500g of diammonium hydrogen phosphate, dissolve it in 2000mL of deionized water to obtain solution A; grind 1000g of petroleum coke to powder, then add it to solution A, leave it for 1.5h, then filter, and put the obtained solid sample in an oven at 110 Dry at ℃ for 5h. At 200°C, use water vapor to pretreat the dried solid sample for 3 hours (the volumetric space velocity of the water vapor gas is 1000h -1 ), then raise the temperature to 400°C, continue pretreatment for 3h, and then cool to 60°C under nitrogen protection to obtain pretreated petroleum coke.

[0051] Mix 1000g of the pretreated petroleum coke obtained above, 62.2g of lanthanum nitrate and 3000g of potassium hydroxide evenly, place in a microwave heating furnace with a microwave frequency of 2450MHz, vacuumize, and heat up to 600 ℃, keep it constant for 20min, then pass nitrogen gas to normal pressure, continue to raise the temperature to 900℃ for 10min under the...

Embodiment 3

[0057] (1) Catalyst preparation

[0058] Weigh 400g of ammonium dihydrogen phosphate, dissolve it in 2000mL deionized water to obtain solution A; grind 1000g of petroleum coke to powder, then add it to solution A, leave it for 1.5h, then filter, and put the obtained solid sample in an oven at 110 Dry at ℃ for 5h. At 200°C, pretreat the dried solid sample with water vapor for 3 hours (the volumetric space velocity of the water vapor gas is 800 hours) -1 ), then raise the temperature to 400°C, continue pretreatment for 3h, and then cool to 60°C under nitrogen protection to obtain pretreated petroleum coke.

[0059] Mix 1000g of the pretreated petroleum coke obtained above, 89.9g of lanthanum nitrate and 4000g of potassium hydroxide evenly, place in a microwave heating furnace with a microwave frequency of 2450MHz, vacuumize, and heat up to 400 under the condition that the microwave power is 0.3kw ℃, keep it constant for 60min, then pass nitrogen gas to normal pressure, continu...

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Abstract

The invention discloses a supported heteropolyacid catalyst and a preparation method thereof. The catalyst comprises an active component, an auxiliary agent and a carrier, wherein the active componentis heteropolyacid, the auxiliary agent is selected from one or more of rare earth elements, and the carrier is petroleum coke-based activated carbon. The preparation method comprises the following steps: mixing petroleum coke, auxiliary-containing metal soluble salt and an activating agent, uniformly mixing, activating, washing and drying; and finally, introducing heteropolyacid, drying and roasting to obtain the supported heteropolyacid catalyst. The catalyst prepared by the method has high low-temperature activity, selectivity and carbon deposition resistance.

Description

technical field [0001] The invention belongs to the field of chemical industry, and relates to a catalytic material and a preparation method thereof, in particular to a supported heteropolyacid catalyst and a preparation method thereof. Background technique [0002] Dimethyl ether (Dimethy Ether, abbreviated as DME) is a colorless, non-toxic gas at normal temperature and pressure, which can be compressed into a liquid. Dimethyl ether is an important organic chemical raw material and chemical intermediate, which can be used in aerosols, refrigerants, alkylating agents, pharmaceuticals, cosmetics, fuels and other industries. [0003] Dimethyl ether was first produced by rectification of by-products in high-pressure methanol production, and soon developed into two processes of methanol dehydration and direct synthesis of synthesis gas. The liquid-phase method of methanol dehydration to produce dimethyl ether, the reaction is carried out in the liquid phase, the main disadvanta...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/188B01J31/26B01J31/16B01J35/10C07C41/09C07C43/04
CPCB01J27/188B01J23/30C07C41/09B01J2523/00B01J35/618B01J35/617B01J35/638B01J35/635C07C43/043B01J2523/3712B01J2523/41B01J2523/69Y02P20/52
Inventor 金浩刘璐朱慧红杨光孙素华杨涛
Owner CHINA PETROLEUM & CHEM CORP
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