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A processing method of an oil-containing waste catalyst discharged from a fluidized bed

The technology of a waste catalyst and a treatment method is applied in the petroleum industry, refined hydrocarbon oil, removal of solid waste, etc., and can solve the problem that there is no good treatment method for the oil-containing waste catalyst discharged from the fluidized bed, so as to achieve harmless treatment, The effect of reducing equipment investment and efficient separation

Active Publication Date: 2015-06-03
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] From the above, it can be seen that there is no good treatment method for the separation of oily waste catalyst discharged from the fluidized bed at present.

Method used

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  • A processing method of an oil-containing waste catalyst discharged from a fluidized bed
  • A processing method of an oil-containing waste catalyst discharged from a fluidized bed
  • A processing method of an oil-containing waste catalyst discharged from a fluidized bed

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Embodiment 1

[0029]The process of producing light oil by using the ebullated bed process with residual oil as raw material, the properties of the raw material are shown in Table 1, the conditions of the ebullated bed hydrogenation process are shown in Table 2, and the catalyst is [give the serial number or specific properties of the product]

[0030] Table 1 The general properties of the raw oil used in the test

[0031]

[0032] Table 2 Fluidized bed hydrogenation process conditions

[0033]

[0034] As the reaction proceeds, when the catalyst activity cannot meet the reaction requirements and a part of the catalyst needs to be unloaded, the oil-containing waste catalyst is discharged through the reactor discharge port. The properties of the oil-containing waste catalyst are shown in Table 3, and the oil-containing waste catalyst enters the first stage The extraction reactor and the secondary extraction reactor carry out the extraction reaction, wherein, the operating conditions of ...

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Abstract

A processing method of an oil-containing waste catalyst discharged from a fluidized bed is disclosed. According to the method, the oil-containing waste catalyst is processed by adoption of two-stage extraction reactors which are connected in series; firstly the oil-containing waste catalyst is directly fed into the first-stage extraction reactor, light hydrocarbons in effluent gas of a cold-high pressure separator of the fluidized bed is adopted as a first-stage extractant, the first-stage extractant and the oil-containing waste catalyst are in contact and subjected to a supercritical extraction reaction, the obtained extract after the reaction is separated to obtain the first-stage extractant and light oil, and the obtained extraction residue is fed into the second-stage extraction reactor; and one or more selected from gasoline obtained by a fractionating system of the fluidized bed, diesel oil obtained by the fractionating system and the light oil obtained by separation of the first-stage extract is adopted as a second-stage extractant, the obtained extract after the reaction is fed into a fractionating system of a fluidized bed reactor or returns to the fluidized bed reactor, and the obtained extraction residue is the waste catalyst. The method can achieve efficient separation of the waste catalyst by utilization of products and properties of a fluidized bed system itself.

Description

technical field [0001] The invention relates to a catalyst treatment method, in particular to a treatment method for oil-containing waste catalyst discharged from a fluidized bed. Background technique [0002] Among the current residual oil hydrogenation processes, the fixed bed residual oil hydrogenation and ebullating bed residual oil hydrogenation technologies are the most mature. In the fixed-bed residue hydrogenation process, the catalyst bed in the fixed-bed reactor is fixed, and the residue raw material and hydrogen are mixed into the reactor from the upper or bottom of the reactor (UFR process), and the hydrogenation is carried out under the set reaction conditions. hydrogen reaction. In the late stage of the reaction, when the device is finished running, in order to avoid the problem of directly stopping the feed, resulting in the remaining unreacted residual oil in the catalyst bed, making it difficult to unload the catalyst, it is generally adopted to add some...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G21/00B09B3/00
Inventor 杨涛孟兆会陈新郭蓉蒋立敬
Owner CHINA PETROLEUM & CHEM CORP
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