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A two-stage heavy oil slurry bed hydrogenation equipment and method

A slurry bed, heavy oil technology, applied in hydrotreating process, treatment of hydrocarbon oil, petroleum industry, etc., can solve the problems of hydrogenation catalyst poisoning, catalyst pore blockage, poor reactor operating conditions, etc., and achieve heavy oil conversion rate. High, improve the compatibility, improve the effect of hydrogenation conversion rate

Active Publication Date: 2019-03-08
CHINA PETROLEUM & CHEM CORP +1
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

At present, the most commonly used in the hydrogenation process is the downflow fixed bed reactor, that is, the trickle bed reactor, but heavy oil products such as residual oil and coal liquefied oil are prone to poisoning of the hydrogenation catalyst or catalyst pores due to high impurity content. Blockage and rapid deactivation, and impurities may block the bed layer, causing a rapid increase in pressure drop, resulting in poor reactor conditions, or even failure to operate normally

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  • A two-stage heavy oil slurry bed hydrogenation equipment and method

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Embodiment 1

[0048] Use as attached figure 1 In the two-stage heavy oil slurry bed hydrogenation equipment shown, in the first and second slurry bed reactors, the diameter ratio of the riser to the outer tube of the downcomer is 2:1, and the diameter ratio of the expansion section to the riser The diameter ratio of the outer cylinder of the slurry phase separator to the expansion section is 0.9:1, and the diameter ratio 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 tapered structure at the lower part of the expansion section, and the interface between the lower part of the riser and the bottom of the downcomer is 2.5m away from the bottom of the riser.

[0049] 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, added t...

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Abstract

The invention discloses a two-stage heavy oil slurry bed hydrogenation device and method. The device comprises a first slurry bed reactor, a first separation unit made communicated with the first slurry bed reactor, a second slurry bed reactor made communicated with the discharge end of the first separation unit, and a second separation unit made communicated with the second slurry bed reactor. The first slurry bed reactor and the second slurry bed reactor each comprises an ascending pipe (4), an expanded section (1) on the top of the ascending pipe, and a descending pipe (8), wherein the expanded section (1) is made communicated with the upper portion of the descending pipe (8), the lower portion of the ascending pipe (4) is made communicated with the bottom of the descending pipe (8), a slurry phase separator is arranged in the expanded section (1), the slurry phase separator is of a sleeve structure composed of an inner sleeve (3) and an outer sleeve (2), the bottom of the ascending pipe (4) is provided with a fluid distributor (7), the bottom of the ascending pipe (4) is provided with a raw material inlet (9), and the top of the expanded section is provided with a material outlet (10). According to the two-stage heavy oil slurry bed hydrogenation device and method, long-period operation of the reactors can be achieved, and the heavy oil hydrogenation conversion rate and the machining efficiency of follow-up equipment for slurry are improved.

Description

technical field [0001] The invention relates to a heavy oil hydrogenation equipment and method, more specifically, to a heavy oil hydrogenation equipment and method using a two-stage slurry bed reactor. 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 the downflow fixed bed reactor, that is, the trickle bed reactor, but heavy oil products such as residual oil and coal liquefied oil are prone to poisoning of the hydrogenation catalyst or catalyst pores due to high impurity content. Blockage and rapid deactivation, and impurities may block the bed layer to cause a rapid increase in pressure drop, resulting in poor working conditions of the reactor, or even failure to operate normally. The react...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G67/02
Inventor 唐晓津张占柱侯栓弟朱振兴胡立峰王子军侯焕娣董明
Owner CHINA PETROLEUM & CHEM CORP