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Hydrocarbon oil hydrogenation depickling catalyst and application thereof

A catalyst and deacidification technology, applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., to achieve the effect of reducing costs and meeting requirements

Active Publication Date: 2013-06-19
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] Although the molecular weight of acid-containing components in some acid-containing hydrocarbon oil feedstocks is relatively small, due to the inclusion of heavy components, these heavy components will block the openings of small pores under reaction conditions, which is not conducive to the production of relatively small molecular weight components. Small acid-containing components enter the catalyst pores for deacidification reaction

Method used

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  • Hydrocarbon oil hydrogenation depickling catalyst and application thereof
  • Hydrocarbon oil hydrogenation depickling catalyst and application thereof
  • Hydrocarbon oil hydrogenation depickling catalyst and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] Take by weighing 70 grams of pseudo-boehmite dry glue (containing 73wt% of alumina) and 50 grams of kaolin respectively, add 1.41 grams of carbon black, 1.41 grams of asparagus powder, mix uniformly, then add 9.78 grams of ammonia water, add 70 grams of distilled water, Carrier A was obtained by kneading and extrusion, drying at 120°C for 2 hours, and calcining at 800°C for 3 hours.

[0020] Weigh 82.11 grams of ammonium heptamolybdate, add 900 ml of ammonia water with a concentration of 12%, then add 27.94 grams of basic nickel carbonate and stir until completely dissolved, adjust the volume of the solution to 1000 ml with ammonia water to obtain solution L-1. Carrier A was saturated and impregnated with solution L-1, dried at 110°C for 2 hours, and calcined at 500°C for 5 hours to obtain catalyst T-A.

Embodiment 2

[0022] The method is the same as in Example 1, except that 1.94 g of basic magnesium carbonate is added, dried at 120° C. for 2 hours, and calcined at 600° C. for 2 hours to obtain carrier B. Carrier B was saturated and impregnated with solution L-1, dried at 120°C for 2 hours, and calcined at 480°C for 3 hours to obtain catalyst T-B.

Embodiment 3

[0024] Take by weighing 40 grams of pseudo-boehmite dry glue (containing alumina 73wt%) and 70 grams of montmorillonite respectively, add 2.52 grams of carbon black, 2.52 grams of turnip powder and 3.52 grams of ammonium carbonate, mix well, then add 65 grams of Distilled water, kneaded and extruded to shape, then dried at 100°C for 3 hours, and calcined at 600°C for 1 hour to obtain carrier C.

[0025] Weigh 53.30 g of ammonium heptamolybdate, add 900 ml of 12% ammonia water, then add 18.14 g of basic nickel carbonate and stir until completely dissolved, adjust the volume of the solution to 1000 ml with ammonia water to obtain solution L-2. Saturated carrier C was impregnated with L-2 solution, dried at 100°C for 6h, and calcined at 520°C for 3h to obtain catalyst T-C.

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Abstract

The invention relates to a hydrocarbon oil hydrogenation depickling catalyst and the application thereof. The hydrogenation depickling catalyst comprises carriers and active metals. The carriers comprise alumina and clay material. The weigh ratio of aluminum and clay material is from 1:99 to 55:45. The active metals comprise metals of VIII group and VIB group. The hydrogenation depickling catalyst preferably comprises magnesium oxide auxiliary agent or zinc oxide auxiliary agent. The invention has the advantages that: the cost is low, the usage performance is good, and the catalyst of the invention is useful in treatment of various heavy acid-containing hydrocarbon oil raw materials. The catalyst of the invention can be applied to the treating process of hydrogenation depickling of acid-containing crude oils, acid-containing heavy oils or acid-containing residual oils.

Description

technical field [0001] The invention relates to a catalyst for hydrogenation treatment of acid-containing hydrocarbon oil and its application, more particularly to a catalyst for hydrogenation-deacidification of acid-containing hydrocarbon oil and its application. Background technique [0002] Acidic substances in petroleum include fatty acids, naphthenic acids, aromatic acids and other substances such as mercaptans, phenols, hydrogen sulfide, inorganic acids, etc., collectively referred to as petroleum acids, accounting for about 1-2% of crude oil, and naphthenic acids account for 1-2% of petroleum. About 90% of acid. Naphthenic acid usually exists in naphthenic crude oil in the form of complex organic acid with five-membered or six-membered saturated ring structure, and its content is less in intermediate base and paraffin base crude oil. The concentration or content of petroleum acid is represented by the total acid value. The total acid number (TAN) refers to the numbe...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/883C10G45/08
Inventor 朱慧红孙素华刘杰杨光张成
Owner CHINA PETROLEUM & CHEM CORP