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Heavy oil hydrogenation slurry bed reactor and heavy oil hydrogenation method

A heavy oil hydrogenation and slurry bed technology, applied in chemical instruments and methods, hydrocarbon oil cracking, petroleum industry, etc., can solve problems such as easy clogging, high impurity content, and inapplicability, and achieve low solid particle content and extended operation The effect of cycle and simple structure

Inactive Publication Date: 2015-04-29
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Because heavy distillate oil is relatively viscous, has high impurity content, and is easy to block, this slurry bed loop reactor is not suitable for heavy oil hydrogenation process

Method used

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  • Heavy oil hydrogenation slurry bed reactor and heavy oil hydrogenation method

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Embodiment 1

[0045] Use as attached figure 1 In the slurry bed reactor shown, the diameter ratio of the riser to the outer tube of the downcomer is 2:1, the diameter ratio of the expansion section to the riser is 2:1, and the diameter ratio of the slurry phase separator outer cylinder to the expansion section is The ratio of the diameter of the inner cylinder to the outer cylinder of the slurry phase separator is 0.6:1. The connection position between the expansion section and the downcomer is the inverted cone structure at the lower part of the expansion section, and the connection between the lower part of the riser and the downcomer is 2.5m away from the bottom of the riser.

[0046] Catalyst preparation method: metal precursor ammonium molybdate ((NH 4 )6Mo 7 o 24 4H 2 O), nickel nitrate (Ni(NO 3 ) 2 ·6H 2 O) and vanadium oxide (V 2 o 5 ) with a mass ratio of 3.3:4.16:1, add it into water, and stir well. Then add acid-treated activated carbon 3.5 times the total mass of the m...

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Abstract

The invention relates to a heavy oil hydrogenation slurry bed reactor and a heavy oil hydrogenation method. The heavy oil hydrogenation slurry bed reactor comprises a riser (4), an expansion section (1) at the top of the riser and a downcomer (8), wherein the expansion section (1) is communicated with the upper part of the downcomer (8), the lower part of the riser (4) is communicated with the bottom of the downcomer (8), a slurry phase separator is arranged in the expansion section (1), the slurry phase separator is of a sleeve structure comprising an inner cylinder (3) and an outer cylinder (2), a fluid distributor (7) is arranged at the bottom of the riser (4), a raw material inlet (9) is formed in the bottom of the riser (4), and a material outlet (10) is formed in the top of the expansion section. The slurry bed reactor provided by the invention is suitable for heavy oil hydrogenation process and can realize hydrogenation reaction to separate a light oil product and an unreacted heavy oil product. The slurry bed reactor provided by the invention can also inhibit the generation of coke particles of a heavy oil reaction system and effectively prolong the operation period of the reactor.

Description

technical field [0001] The invention relates to a slurry bed reactor and its application method, more specifically, to a slurry bed loop reactor suitable for heavy oil hydrogenation process and a heavy oil hydrogenation method. Background technique [0002] Hydrogenation is an important technical route for the treatment of inferior raw materials. Through hydrogenation, impurities such as metals, colloids, residual carbon, sulfur, and nitrogen in heavy oil products can be effectively removed. At present, the most commonly used in the hydrogenation process is a downflow fixed bed reactor, that is, a trickle bed reactor. However, due to the high content of impurities in heavy oil products (such as residual oil and coal liquefied oil), it is easy to cause hydrogenation catalyst poisoning or Catalyst pores are clogged and deactivated quickly, and impurities may clog the bed layer, causing a rapid increase in pressure drop, resulting in poor working conditions of the reactor, or e...

Claims

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Application Information

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IPC IPC(8): B01J8/20C10G47/26
CPCB01J8/22C10G47/26C10G2300/1037C10G2300/107C10G2300/1077
Inventor 唐晓津张占柱胡立峰朱振兴侯栓弟王子军
Owner CHINA PETROLEUM & CHEM CORP