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A kind of heavy oil hydrotreating method

A treatment method and heavy oil hydrogenation technology, applied in the directions of hydrotreating process, treatment of hydrocarbon oil, chemical instruments and methods, etc., can solve the problems such as the inability of the catalyst to play effectively, and achieve easy implementation, low energy consumption, repeatability and high efficiency. good controllability

Active Publication Date: 2019-07-23
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The purpose of the present invention is to overcome the shortcomings of various catalysts in the existing heavy oil hydrotreating method, and to provide a catalyst that can achieve comprehensive demetallization, desulfurization, and residual carbon removal effects and is not easy to form carbon deposits and has high stability. Proactive heavy oil hydrotreating method

Method used

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  • A kind of heavy oil hydrotreating method
  • A kind of heavy oil hydrotreating method
  • A kind of heavy oil hydrotreating method

Examples

Experimental program
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Effect test

Embodiment approach

[0019] According to a preferred embodiment of the present invention, the modified carrier is prepared by a method comprising the following steps:

[0020] (1) impregnating the hydrothermally treated carrier in an alkaline solution A containing a metal additive compound providing the metal additive, and then drying;

[0021] (2) impregnating the carrier obtained in step (1) in the acidic solution B containing the acidic additive compound providing the acidic additive, then drying and calcining.

[0022] In the preparation method of the above-mentioned modified support, the inventors of the present invention have found through in-depth research that before impregnating the solution A containing the metal additive compound, the support is subjected to hydrothermal treatment, and the impregnation of the two impregnations is controlled. The acidity and alkalinity of the liquid can make the metal additives mainly distributed in the shell layer of the carrier, while the acidic additive...

preparation example 1

[0092]This preparation example is used to illustrate the preparation process of the alumina carrier used in the present invention.

[0093] Take by weighing 1000 grams of dry rubber powder produced by Changling Catalyst Factory (the dry basis is 71% by weight, wherein the content of pseudoboehmite is 68% by weight, the content of trihydrate alumina is 5% by weight, and the balance is amorphous alumina ), 30 grams of Tianjing powder (product of Henan Lankao Tianjing Rubber Factory) and 30g of hydroxymethyl cellulose and mix evenly, then add 1200 milliliters of aqueous solution containing 28g of nitric acid, and extrude on a plunger type extruder into an outer diameter of 2.5 mm, a Raschig ring bar with an inner diameter of 1mm. Then the wet Raschig strip was dried at 120° C. for 4 hours, and then fired at 960° C. for 3 hours to obtain the protective agent carrier Z1. Measured by the BET method, the pore volume of the protective agent carrier Z1 is 0.95mL / g, and the specific su...

Embodiment 1

[0097] This example is used to illustrate the heavy oil hydrotreating method provided by the present invention.

[0098] (1) Preparation of modified carrier

[0099] (1-1) Take 200 grams of the carriers Z1, Z2 and Z3 prepared in Preparation Example 1, firstly treat the carriers at 135°C for 12 hours with hydrothermal treatment, and then use 165 ml of hydrothermally treated carriers with a temperature of 40°C containing 15 g / L Mg(NO 3 ) 2 The aqueous solution (pH value is 11) is saturated and impregnated for 1 hour, and then dried at 200 ° C for 8 hours to obtain a carrier loaded with metal additives;

[0100] (1-2) The carrier obtained in step (1) is loaded with metal additives in 145 milliliters of 40 ° C containing 10 g / L H 3 BO 3 Soaked in an aqueous solution (pH value of 6) for 1 hour, then dried at 120°C for 3 hours, and then calcined at 400°C for 3 hours to obtain modified supports S1-1, S2-1, and S3-1.

[0101] (2) Preparation of protective agent, demetallization a...

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Abstract

The invention relates to the field of petrochemical engineering, and discloses a heavy oil hydrotreatment method. The method includes the following steps: under the condition of hydrogenation reaction, a heavy oil material is sequentially put in contact with a protective agent, a demetallization agent and a desulfurizing agent, the protective agent, the demetallization agent and the desulfurizing agent respectively contain a catalyst carrier and an active metal component loaded in the catalyst carrier, wherein the catalyst carrier of at least one of the protective agent, the demetallization agent and the desulfurizing agent is a modified carrier, the modified carrier contains an acid additive and a metal additive distributed in the carrier in a layering manner, the acid additive is distributed in the core layer, and the metal additive is distributed in the shell layer. The heavy oil hydrotreatment method provided by the invention not only can achieve a higher metal, sulfur and carbon residue removal effect, more praiseworthily, the catalyst stability is high, the running time is long, and thereby the heavy oil hydrotreatment method provided by the invention has a better industrial application prospect.

Description

technical field [0001] The invention relates to the field of petrochemical industry, in particular to a heavy oil hydrotreating method. Background technique [0002] The deep processing of heavy oil including residual oil is not only conducive to improving the utilization rate of heavy oil and alleviating the tense trend of energy supply, but also reducing environmental pollution and achieving clean utilization of energy. Due to the characteristics of high density and high heteroatom content of residual oil, it is difficult for one catalyst to meet the requirements of removing various heteroatoms and is easy to deactivate. Therefore, the residual oil hydrogenation catalyst usually adopts a graded system. The particle size and particle size gradually decreased, while the hydrogenation activity of the catalyst gradually increased. Carbon deposition and metal deposition are the main factors causing the deactivation of residual oil hydrogenation catalysts, and studies have show...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G65/04B01J23/888B01J23/887B01J32/00
CPCB01J23/002B01J23/8872B01J23/888B01J2523/00C10G65/04C10G2300/202C10G2300/205C10G2300/70B01J2523/847B01J2523/845B01J2523/68B01J2523/69B01J2523/22
Inventor 贾燕子杨清河李大东刘学芬邓中活刘涛
Owner CHINA PETROLEUM & CHEM CORP