Method for producing high-quality diesel oil with low condensation point

A diesel and low-condensation technology, which is applied in the petroleum industry, hydrocarbon oil treatment, hydrotreating process, etc., can solve the problems of cycle limitation, large temperature drop, and high reaction temperature at the outlet of the bed, so as to reduce the overall temperature gradient and ensure quality and yield, the effect of lowering the hot spot temperature

Active Publication Date: 2014-05-21
CHINA PETROLEUM & CHEM CORP +1
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  • Abstract
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Problems solved by technology

In this method, the temperature drop in the bed of the hydrodepreciation catalyst is relatively large, and the yield of the diesel fraction and the improvement of the depreciation effect are limited to a certain extent, which reduces the service life of the hydrodecondensation catalyst.
[0006] CN102051232A introduces a method for diesel hydrotreating decondensation, which ha

Method used

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  • Method for producing high-quality diesel oil with low condensation point

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Example Embodiment

[0035] Example 1

[0036] use figure 1 The shown process flow uses grading and mixing in series to produce low freezing point high-quality diesel. Example 1 includes two series-connected hydrogenation reaction zones, and the mixing volume ratio of the hydrotreating catalyst and the hydropour point depressurization catalyst in each reaction zone is 1:4. The hydrorefining catalyst used in Example 1 was a FH-98 catalyst, the hydrogenation-upgrading isomerized pour point depressant catalyst was an FC-14 catalyst, and the hydrogen-promoting catalyst was an FDW-3 catalyst, and the catalysts were all Fushun Petrochemical Co., Ltd. The commercial catalyst developed and produced by the research institute.

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Abstract

The invention discloses a method for producing high-quality diesel oil with a low condensation point. The method comprises the following steps: mixing a diesel oil raw material with hydrogen, orderly passing through at least two hydrogenation reaction zones connected in series, wherein in the material flowing direction, each hydrogenation reaction zone orderly comprises a hydro-refining dewaxing composite catalyst bed layer filled with a mixture of a hydrodewaxing catalyst and a hydro-refining catalyst, and a hydro-upgrading isodewaxing catalyst bed layer; performing separation and fractionation of the reaction effluent from the last hydrogenation reaction zone to obtain the diesel oil product with a low condensation point. The method of the invention reasonably combines and utilizes the temperature increase of the hydro-refining and hydro-upgrading dewaxing process with the temperature decrease of the hydrodewaxing process, improves the diesel oil yield and the cetane value while producing diesel oil with a low condensation point and low sulfur, reduces the hot-spot temperature of the device, prolongs the running period, also reduces the cold hydrogen consumption or the combustion gas loss of a heating furnace, and saves operation cost.

Description

technical field [0001] The invention relates to a method for producing high-quality low-condensation diesel, in particular to a hydrogenation method for producing low-condensation diesel through catalyst grading technology and composite filling technology. Background technique [0002] Diesel, as a fuel for compression ignition engines, plays an irreplaceable role as a non-renewable resource in modern production and life, and can be used as vehicles, tanks, airplanes, tractors, railway vehicles and other vehicles or other machinery Fuel can also be used for power generation, heating, etc. Depending on the industry and environment in which it is used, the quality requirements of users for diesel products are also very different. For people living in alpine regions or in winter, the demand for low-condensing-point diesel has always been high. The traditional choice The cracking process can process waxy heavy diesel fractions, and the pour point depressing range can reach 20-5...

Claims

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Application Information

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IPC IPC(8): C10G67/02
Inventor 孙薇彭冲石友良黄新露吴子明廖娜王仲义
Owner CHINA PETROLEUM & CHEM CORP
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