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A Flexible Diesel Hydrogenation Upgrading and Depressing Process

A technology for hydro-upgrading and hydro-pump reduction, which is applied in hydrotreating process, petroleum industry, treatment of hydrocarbon oil, etc., can solve the problems of single product, low pour point of diesel products, and inability to meet low pour point diesel oil, etc. Achieving the effect of high cetane number

Active Publication Date: 2021-07-09
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Distillate fraction hydrotreating and depreciating technologies, such as CN102051232A and CN1257107A, etc., use hydrorefining catalysts and hydrotreating depreciating catalysts, and adopt a series of processes to produce low-condensing point diesel products, but the yield of diesel products is low
CN102453531A, CN103805258A and CN103805254A all alternately use hydrotreating catalysts and hydrotreating pour point depressing catalysts to obtain diesel products with low freezing point, but the yield of diesel oil is also low, and only one kind of diesel product can be produced
[0005] CN1415705A is a high-quality diesel production method using combined hydrogenation technology. The raw material oil is subjected to gas-liquid separation after hydrofining and hydrodecondensation, and the liquid product is hydrogenated and dearomatized using a noble metal catalyst. Due to the use of a two-stage process, The process is complicated and only one diesel product can be produced
[0006] To sum up, the existing diesel hydrotreating technology can obtain a higher yield of diesel products, and the product quality is greatly improved, such as cetane number, sulfur content, aromatics content, density, etc., but the freezing point is lowered The range is not large or does not decrease, which cannot meet the requirements of low pour point diesel oil
The existing hydrogenation decondensation technology can greatly reduce the freezing point of diesel products, which can meet the index requirements of low-condensing diesel, but the yield of diesel is low, usually less than 90m%, and the quality of diesel products is not greatly improved. When high cetane number n-paraffins are cracked into gas or naphtha fractions, the cetane number of diesel products will be reduced
When combined hydrogenation technology is used, the process is complicated and the product is single
There is only one kind of diesel product produced by the above process technology, and the product flexibility is poor

Method used

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  • A Flexible Diesel Hydrogenation Upgrading and Depressing Process
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  • A Flexible Diesel Hydrogenation Upgrading and Depressing Process

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Embodiment 1-4

[0039] Protective agents FZC-100, FZC-105 and FZC106 are hydrogenation protective agents developed and produced by Fushun Petrochemical Research Institute of China Petrochemical Corporation; catalyst FHUDS-5 is developed and produced by Fushun Petrochemical Research Institute of China Petrochemical Corporation Hydrofining catalyst; Catalyst 3963 is a hydrogenation upgrading catalyst developed and produced by Fushun Petrochemical Research Institute of China Petrochemical Corporation, containing Y-type molecular sieve; the content of Y-type molecular sieve in 3963B catalyst is higher than the content of Y-type molecular sieve in 3963 catalyst 4 percentage points (number) higher, and the others remain unchanged; Catalyst 3881 is a hydrogenation decondensation catalyst developed and produced by Fushun Petrochemical Research Institute of China Petroleum & Chemical Corporation, containing ZSM-5 molecular sieve.

[0040] Table 1 Main properties of diesel feedstock oil

[0041]

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Abstract

The invention discloses a process for hydrogenation, upgrading and pour point reduction of flexible diesel oil. After the diesel raw material is hydrogenated and refined, it enters the hydrogenation upgrading reactor, and the material passing through the upper hydrogenation upgrading catalyst bed is divided into two strands; one strand of material is extracted from the upgrading reactor through the middle of the bed, and enters the hydrogenation downgrading reactor. The decondensation reaction is carried out in the condensing reactor; another stream of material continues to flow downward through the lower hydrogenation modification catalyst bed; specifications of diesel products. The present invention provides for the first time a hydrogenation upgrading process for simultaneous production of two or more diesel products of different specifications on a set of hydrogenation process equipment, which can make full use of the heat carried by part of the upgrading materials to realize the hydrogenation decondensation reactor Coupling operation with hydro-upgrading reactor.

Description

technical field [0001] The invention belongs to the field of petroleum refining, and in particular relates to a diesel hydrogenation upgrading and pour point depressing process for flexibly producing high-quality diesel products. Background technique [0002] The increasingly stringent environmental protection regulations require higher and higher quality diesel products, mainly due to the increasing restrictions on sulfur content, cetane number, density and polycyclic aromatic hydrocarbon content. Low-quality diesel hydro-upgrading technology can greatly reduce the sulfur content and aromatics content of diesel products, reduce density and increase cetane number. In addition, in winter, diesel products in cold regions have different restrictions and requirements on the freezing point. According to the freezing point, diesel products in my country can be divided into 5#, 0#, -10#, -20#, -35# and -50 # and other different specifications. Hydrogenation decondensation technolo...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G67/00
CPCC10G67/00C10G2300/1055C10G2300/1059C10G2300/307C10G2400/04
Inventor 刘涛方向晨李宝忠赵玉琢李扬孙洪江
Owner CHINA PETROLEUM & CHEM CORP
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