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Deferrization method for hydrocarbons raw oil

A technology for raw material oil and iron removal, applied in the field of iron removal, can solve the problems of increased carbon residue in the regenerated catalyst, reduced catalyst activity, increased SOx emission, etc., and achieves the effect of good iron removal effect and strong iron ion chelating ability.

Active Publication Date: 2012-08-01
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The serious impact of the increase of contaminated iron on the catalytic cracking equilibrium catalyst is manifested in the decrease of catalyst activity and the decrease of residual oil cracking ability, the increase of SOx emission and the increase of carbon residue of regenerated catalyst (for partial regeneration), and the decrease of apparent bulk density of catalyst, etc.
In the hydrogenation process of residue oil and distillate oil hydrotreating process, the iron ions in distillate oil and residue oil cause the catalyst activity to decrease or even deactivate

Method used

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  • Deferrization method for hydrocarbons raw oil
  • Deferrization method for hydrocarbons raw oil
  • Deferrization method for hydrocarbons raw oil

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] Mixed acid (maleic acid, citric acid, EDTA prepared at a molar ratio of 1:1:1) and ammonia water are used to make a deferrification agent (the molar ratio of carboxylic acid to ammonia is 1:1), and the raw material oil is crude oil containing 41ppm iron , and the results are shown in Table 1.

Embodiment 2~4

[0026] Three different organic acids (polyacrylic acid, citric acid, and oxalic acid) were mixed with ethylenediamine at a molar ratio of 2:1 to prepare a deferrification agent, and the deferrification effect was investigated. The raw material oil was crude oil containing 32ppm iron, and the results are shown in the table 2.

Embodiment 5~7

[0032] The iron-removing effect of the iron-removing agent prepared by mixing citric acid and tetraethylenepentamine at a molar ratio of 3:1 was compared at different reaction temperatures. The raw material oil was coked diesel oil containing 29 ppm iron. The results are shown in Table 3.

[0033] Table 3 Iron removal effect of coked diesel oil at different reaction temperatures

[0034]

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PUM

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Abstract

The invention provides a method for removing iron from hydrocarbon feed oil, which comprises the following steps: (1) fully mixing iron-containing hydrocarbon feed oil with iron removing agent solution and reacting; and (2) separating oil-water mixture to remove the majority of iron in hydrocarbon feed oil. The iron removing agent contains a component A and a component B, wherein the component A is selected from one or more of C2 to C6 polycarboxylic acids, C2 to C8 hydroxycarboxylic acids and water-soluble maleic acid and acrylic acid polymer; and the component B is selected from one or moreof ammonia, inorganic or organic ammonium compound, C2 to C8 linear alkyl-amines, cycloalkyl amines or alcohol amines, and polyethylene-polyamines with molecular weight of 100 to 5,000. The iron removing agent prepared from nitrogen-containing compound and organic acid by mixing has higher iron ion chelating ability and can achieve better iron removal effect in shorter reaction time and at lower reaction temperature.

Description

technical field [0001] This invention relates to a process for removing iron from hydrocarbon feed oils. Background technique [0002] In recent years, with the continuous increase in the processing of sour crude oil, high acid crude oil and residual oil, the iron poisoning of catalytic cracking catalysts has attracted more and more attention. The serious impact of the increase of contaminated iron on the catalytic cracking equilibrium catalyst is manifested in the decrease of catalyst activity and the decrease of residual oil cracking ability, the increase of SOx emission and the increase of carbon residue of regenerated catalyst (for partial regeneration), and the decrease of apparent bulk density of catalyst, etc. . During the hydrogenation process of residual oil and the hydrofining process of distillate oil, the iron ions in distillate oil and residual oil cause the catalyst activity to decrease or even deactivate. [0003] Iron exists in the form of suspended inorgan...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G29/20
Inventor 罗咏涛徐振洪于丽
Owner CHINA PETROLEUM & CHEM CORP
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