Preparation and application of a C5/C6 normal paraffin isomerization catalyst

A technology of n-alkane and catalyst, which is applied in the application field of catalyst in the isomerization reaction of C5/C6 n-alkane, and can solve the problems of catalyst trial and effect being difficult to apply and consider, high equipment requirements, and small molecular weight, etc. Achieving clearly innovative, low-cost, mild-condition results

Inactive Publication Date: 2018-05-04
CHINA UNIV OF PETROLEUM (EAST CHINA)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

but C 5 / C 6 Due to the short carbon chain and small molecular weight of mixed alkanes, C 5 / C 6 There is a major difference between the isomerization of mixed alkanes and the isomerization of long-chain alkanes, and the trial and effect of the catalyst are difficult to apply and consider
Moreover, in the preparation process of the patented catalyst, it needs to be calcined at 500°C for 4 hours to prepare the catalyst precursor. The preparation process requires high temperature, high equipment requirements, complicated process, high energy consumption and high cost.

Method used

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  • Preparation and application of a C5/C6 normal paraffin isomerization catalyst
  • Preparation and application of a C5/C6 normal paraffin isomerization catalyst
  • Preparation and application of a C5/C6 normal paraffin isomerization catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] Embodiment 1. At first 8.4g of sodium hypophosphite monohydrate was added to 50mL of deionized water under stirring at room temperature, and after dissolving, 9.4g of nickel chloride hexahydrate was added (the phosphorus / nickel mol ratio was 2 at this moment). After stirring and dissolving, the obtained clear solution was put into a petri dish and dried at 90°C. Then heat-treat the dried precursor powder at 150° C. to 300° C. for more than half an hour under airtight conditions, and cool to room temperature to obtain a black solid. Wash with water more than 3 times. Pour the black solid into an evaporating dish, put it into an oven, and dry it at 80°C, and then the active phase nickel phosphide is obtained.

[0035] Weigh 12g H-Beta molecular sieve powder, 4gγ-Al 2 o 3 Add the powder into a mortar, grind and mix well. Weigh 0.64g of the above-prepared nickel phosphide, add it evenly in multiple times, and grind evenly. Spray an appropriate amount of acetic acid solut...

Embodiment 2

[0037] The preparation process of embodiment 2. catalyzer is the same as embodiment 1, and difference is that the phosphorus / nickel mol ratio of the sodium hypophosphite and nickel salt mixed solution adopted in the preparation catalyzer process is 5, and active phase phosphating in the prepared catalyzer The mass fraction of nickel is 4%. The implementation conditions of the n-hexane hydroisomerization of the catalyst are the same as in Example 1. As a result of the analysis, the conversion rate of n-hexane was 78.1%, and the isomerization selectivity was 89.7%.

Embodiment 3

[0038] The preparation process of embodiment 3. catalyzer is the same as embodiment 1, and difference is that the phosphorus / nickel mol ratio of the sodium hypophosphite and nickel salt mixed solution adopted in the preparation catalyzer process is 1, and active phase phosphating in the prepared catalyzer The mass fraction of nickel is 4%. The implementation conditions of the n-hexane hydroisomerization of the catalyst are the same as in Example 1. As a result of the analysis, the conversion rate of n-hexane was 81.3%, and the isomerization selectivity was 85.6%.

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Abstract

The invention discloses a preparation method of an isomerization catalyst using nickel phosphide prepared by a low-temperature thermal reduction method as an active phase, and is applied to catalyze the isomerization of C5 / C6 normal alkanes. The carrier of the catalyst is H-Beta molecular sieve, the active phase is nickel phosphide obtained by low-temperature thermal reduction of hypophosphite and nickel salt, and the catalyst is obtained by dry mixing nickel phosphide and molecular sieve. The mass of nickel phosphide accounts for 1% to 10% of the total mass of the catalyst. The method of applying the catalyst to the isomerization of C5 / C6 alkanes is as follows: fill the prepared catalyst in the fixed bed reactor, and feed the catalyst according to the molar ratio of hydrogen to normal alkanes (n(H2 / Cn)) at 1 to 6:1, The reaction temperature is 250°C-350°C, the reaction pressure is 1-4MPa, and the mass space velocity of normal alkanes is 0.5-5h-1, and the isomerization reaction is carried out. The catalyst involved in the invention has the advantages of easy preparation, low cost, high activity, good stability, etc., and has good application prospects.

Description

technical field [0001] The present invention relates to a kind of nickel phosphide produced by hypophosphite and nickel salt low-temperature thermal reduction method as active phase, the preparation of catalyst with H-Beta molecular sieve as carrier, and the catalyst prepared in C 5 / C 6 Application in the isomerization reaction of normal alkanes. Background technique [0002] At present, the main source of gasoline in my country is catalytic cracking gasoline, in which the content of olefins and aromatics is relatively high. In the past, they have been used as components to maintain the high octane number of gasoline, and have not been strictly restricted. However, as relatively active hydrocarbons, olefins are not stable in themselves. Not only are they prone to react to form colloids and carbon deposits, which affect the stability of gasoline, but also cause environmental pollution; and aromatics can also cause carcinogen emissions and affect human health. With the incr...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/76C07C5/27C07C9/16C07C9/18
Inventor 夏道宏刘咸尚朱丽君项玉芝周玉路
Owner CHINA UNIV OF PETROLEUM (EAST CHINA)
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