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A kind of precious metal hydrogenation catalyst and its preparation method and application

A hydrogenation catalyst and precious metal technology, which is applied in the field of alumina-based precious metal paraffin deep refining catalyst and its preparation, can solve the problems of product quality not meeting the requirements, and achieve the effect of improving sulfur resistance and anti-coking performance

Active Publication Date: 2017-03-22
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The above existing paraffin hydrogenation technologies generally have the problem that the product quality cannot meet the requirements during long-term operation

Method used

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  • A kind of precious metal hydrogenation catalyst and its preparation method and application
  • A kind of precious metal hydrogenation catalyst and its preparation method and application
  • A kind of precious metal hydrogenation catalyst and its preparation method and application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] (1) Roast kaolin raw soil in a high-temperature furnace at a temperature of 600°C and keep the temperature for 4 hours. After cooling, weigh 30g and put it into a container, add 150mL of 2mol / L nitric acid and 150mL of 2mol / L citric acid, and heat for reaction. The reaction temperature is 60°C, and the reaction time is 8h;

[0032] (2) Add 30g of Y-type molecular sieve to the modified kaolin slurry, then add 700mL of distilled water, the solid content in the slurry is 6wt%, heat to 70°C, and the prepared concentration is 46gAl 2 o 3 / L of sodium metaaluminate and a concentration of 15gAl 2 o 3 / L aluminum sulfate solution is added to the modified kaolin slurry in parallel, and the pH is controlled to 8.5. The temperature is kept at 70°C during the gelation process. (OP-10) 40mL, aging time 40 minutes, the aged slurry was washed with 70°C deionized water until neutral, and dried at 120°C for 3 hours to obtain silicon-containing alumina dry glue A;

[0033] (3) Weigh ...

Embodiment 2

[0036] Other conditions are the same as in Example 1, except that the amount of the mixture of ethyl acetoacetate and acetic acid is changed to 25g (including 5g of ethyl acetoacetate and 20g of acetic acid). Catalyst product number B.

Embodiment 3

[0038] Other conditions are with embodiment 1, just replace ethyl acetoacetate with butyl acetoacetate, replace acetic acid with succinic acid. Catalyst product number C.

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Abstract

The invention discloses a preparation method of a precious metal hydrogenation catalyst. The preparation method comprises the following steps: (1) roasting the original clay soil at high temperature, then enabling the roasted original clay soil to react with mixed acid, and pulping to prepare slurry, wherein the mixed acid is a mixture of strong acid and weak acid; (2) adding a Y type molecular sieve to the slurry in the step, stirring uniformly, adding an aluminum-containing acid solution and an alkaline solution under a parallel flow condition, carrying out a gel forming reaction, and after gel forming, carrying out ageing, filtering, washing and drying to obtain silicon-containing alumina powder; (3) adding an adhesion agent to the silicon-containing alumina powder prepared in the step (2), and carrying out extrusion molding, drying and baking to obtain a silicon-containing alumina supporter; (4) preparing a noble metal aqueous solution containing esters and organic acid, adding the supporter prepared in the step (3) to the solution to be impregnated, and after impregnation, drying and roasting to obtain the precious metal hydrogenation catalyst. The catalyst has the advantages of small active component crystal grain, low dispersity, low strong acid center and the like; the catalyst can be used for paraffin hydrogenation production to produce a food-grade paraffin product.

Description

technical field [0001] The invention relates to a noble metal hydrogenation catalyst and its preparation method and application, in particular to an alumina-based noble metal paraffin deep refining catalyst for hydrogenation and its preparation method and application. Background technique [0002] With the heavy and inferior quality of crude oil and the increasing quantity of imported crude oil, the sources of paraffin hydrorefining raw materials are diversified. Coupled with factors such as the use of various additives in the oil recovery process and the fluctuations in the production process of some refineries, the quality of paraffin wax raw materials has become more and more obvious. At the same time, with the birth of the new paraffin wax standard, the smell of food-grade paraffin wax has been reduced from 1 to 0 in the original standard. Some refineries use clay for supplementary refining or pre-refining, resulting in an increase in processing costs and a decrease in p...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/89C10G73/44
Inventor 张艳侠包洪洲付秋红段日霍稳周陈明乔凯
Owner CHINA PETROLEUM & CHEM CORP