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Method and system for combined processing of deoiled asphalt and aromatic-rich distillate oil

A deoiled bitumen and combined processing technology, which is applied to a system for combined processing of deoiled bitumen and aromatic-rich distillate oil, and the field of combined processing of deoiled bitumen and aromatic-rich distillate oil, can solve the problem of low propylene yield, difficult transportation and utilization, Restrictions on promotion, etc.

Active Publication Date: 2021-05-04
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] In order to solve this problem, the residual oil solvent deasphalting (demetallization)-hydrotreating-catalytic cracking combined process technology (SHF) developed by Sinopec Petrochemical Research Institute is to maximize the production of vehicle-use oil from low-value vacuum residue An innovative technology that cleans fuel and prolongs the operating cycle, but due to the high softening point of deoiled asphaltenes (DOA), it is difficult to transport and utilize, which limits the promotion of SHF technology
[0005] The new combined process of residuum hydrogenation-catalytic cracking (DCC) producing more propylene in the transition to chemical industry is also limited by the influence of asphaltenes and metals in the residuum, the hydrogen content of the hydrogenated residuum is low, and the The operation cycle is short and the DCC propylene yield is low, which affects the economic benefits of the combined technology

Method used

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  • Method and system for combined processing of deoiled asphalt and aromatic-rich distillate oil
  • Method and system for combined processing of deoiled asphalt and aromatic-rich distillate oil
  • Method and system for combined processing of deoiled asphalt and aromatic-rich distillate oil

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specific Embodiment approach

[0073] The conditions of the first hydrogenation unit of deasphalted oil (DAO) in the presence of hydrogen are generally as follows: the hydroprocessing technology of DAO is a fixed-bed hydroprocessing technology. Taking the relatively mature fixed-bed heavy and residual oil hydrogenation technology in the industry as an example, the reactor or reaction bed includes at least two hydrogenation catalysts, and the heavy residue hydrogenation catalyst used refers to the hydrogenation catalyst with heavy and residual oil A combined catalyst with the functions of hydrodemetallization, hydrodesulfurization, hydrodenitrogenation and hydrodecarbonization. These catalysts are generally supported by porous refractory inorganic oxides such as alumina, and oxides or sulfides of Group VIB and / or Group VIII metals such as W, Mo, Co, Ni, etc., as active components. Catalysts added with various additives such as P, Si, F, B and other elements, such as RDM, RCS series heavy and residual oil hyd...

Embodiment A

[0139] Preparation of rich ore precursor material 1: Select 2000g of RPB110 pseudoboehmite produced by Changling Branch of Sinopec Catalyst Co., Ltd., of which 1000g was treated at 550°C for 2h to obtain about 700g of alumina, and about 700g of alumina and another 1000g of pseudoboehmite Mix the boehmite thoroughly, then add 40g of scallop powder and 20g of citric acid, and add 2200g of deionized water, knead and extrude into strips, dry at 300°C for 3 hours to obtain about 1730g of carrier, add 2100mL of Mo and Ni-containing The solution is saturated impregnated, and the Mo content in the solution is expressed as MoO 3 The mass is 5.5%, the Ni content is 1.5% by NiO mass, dipped for half an hour, and then treated at 180°C for 4 hours to obtain the rich ore precursor material 1, the properties of which are shown in Table 7.

[0140] Preparation of rich ore precursor material 2: Select 2000g of RPB110 pseudo-boehmite produced by Sinopec Catalyst Co., Ltd. Changling Branch, add ...

Embodiment B

[0143] A vacuum residue is used as a raw material for solvent deasphalting, and the solvent used is a hydrocarbon mixture with a butane content of more than 70% by weight. At 120°C, the solvent:vacuum residue=3:1 (mass ratio) Solvent deasphalting is carried out under the conditions, the mass yield of DAO is 70%, and the mass yield of DOA is 30%.

[0144] The properties of the obtained DAO and DOA are shown in Table 1.

[0145] The properties of the obtained DAO and DOA are shown in Table 1.

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Abstract

The invention relates to the field of hydrocarbon oil processing, and discloses a method and system for combined processing of deoiled asphalt, and the method comprises the following steps: (11) carrying out solvent deasphalting treatment on heavy raw oil; (12) carrying out hydrogenation reaction on the deasphalted oil, and introducing liquid phase effluent into a DCC unit for reaction; (2) carrying out hydrogenation saturation on the aromatic-rich distillate oil containing LCO and / or HCO, and then fractionating; (3) mixing the deoiled asphalt and the aromatic hydrocarbon-containing material flow with hydrogen, and then carrying out hydrogenation reaction; (4) fractionating the liquid-phase product; (51) reacting the second light component to obtain at least one product selected from a gasoline component, a diesel component and a BTX raw material component; and (52) reacting the second heavy component to obtain at least one product selected from the group consisting of coker gasoline, coker diesel, coker gas oil and low sulfur petroleum coke; or using the second heavy component as a low-sulfur marine fuel oil component. The treatment process provided by the invention can realize high-value utilization of DOA.

Description

technical field [0001] The invention relates to the field of hydrocarbon oil processing, in particular to a method for jointly processing deoiled asphalt and aromatic-rich distillate oil and a system for jointly processing deoiled asphalt and aromatic-rich distillate oil. Background technique [0002] Efficient conversion of residual oil is the core of refinery enterprises. Fixed-bed residual oil hydrogenation is a key technology for efficient conversion of residual oil, which has the characteristics of good product quality and mature technology. [0003] However, the high content of asphaltenes and metals in the residual oil is a restrictive factor for the operation period of the fixed bed residual oil hydrogenation unit. [0004] In order to solve this problem, the residual oil solvent deasphalting (demetallization)-hydrotreating-catalytic cracking combined process technology (SHF) developed by Sinopec Petrochemical Research Institute is to maximize the production of vehi...

Claims

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Application Information

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IPC IPC(8): C10G69/00
CPCC10G69/00C10G2400/02C10G2400/04C10G2400/30C10G2300/1077C10G2300/107C10G2300/202C10G2300/205C10G2300/201
Inventor 杨清河贾燕子牛传峰孙淑玲胡大为戴立顺王振任亮户安鹏
Owner CHINA PETROLEUM & CHEM CORP
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