A kind of hydrocracking method for producing low pour point diesel oil

A technology for hydrocracking and diesel oil, which is applied to chemical instruments and methods, hydrocarbon oil cracking, and hydrocarbon oil treatment. It can solve the problems of complex preparation process, increased preparation cost, and influence on the conversion of aromatics, and achieves simple preparation process and hydrothermal Excellent stability and low production cost

Active Publication Date: 2019-04-12
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method uses expensive surfactants to prepare Y-type molecular sieves, and the preparation process is complicated, which greatly increases the preparation cost
[0009] CN97116250.6 discloses a kind of Y-type molecular sieve, the raw material that this Y-type molecular sieve adopts is common NaY former powder, first carries out ammonium exchange, removes NaY + , and then carried out two hydrothermal treatment and acid treatment, the distribution of pores larger than 2nm in the modified Y-type molecular sieve obtained was 40%~66% of the total pore volume, which affected the conversion of macromolecular aromatics in the raw material, and the prepared catalyst product Distribution and product quality need to be further improved

Method used

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  • A kind of hydrocracking method for producing low pour point diesel oil
  • A kind of hydrocracking method for producing low pour point diesel oil
  • A kind of hydrocracking method for producing low pour point diesel oil

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0065] In this example, large-grain NaY molecular sieves were prepared by the method of the present invention.

[0066] Preparation of LY-1

[0067] (1) Preparation of gel: Slowly add 165mL of water glass to 63mL of high alkali sodium metaaluminate solution under stirring condition at a temperature of 25°C. After mixing evenly, add 42.5mL of aluminum sulfate solution and 35.6mL of low Alkaline sodium metaaluminate solution, stirred at constant temperature for 0.5 hours, and then aging the obtained synthetic solution at the above temperature for 1 hour to obtain a gel;

[0068] (2) Crystallization: Under stirring conditions, raise the gel in the synthesis kettle to 100°C at a heating rate of 2.5°C / min, stir and crystallize at a constant temperature for 16 hours, after the crystallization is completed, quickly cool down with cold water, and open the The synthesized molecular sieve was taken out from the synthesis kettle, and the product LY-1 was obtained after filtering, washin...

Embodiment 2

[0083] Firstly, ammonium exchange is carried out on the raw material large-grain NaY molecular sieve LY-1. Prepare 10 liters of 0.5 mol / L ammonium nitrate aqueous solution. Weigh 2,000 grams of small-grain NaY molecular sieves, dissolve them in 10 liters of prepared ammonium nitrate aqueous solution, stir at 90°C for 1 hour at a constant temperature of 300 rpm, then filter the molecular sieves, and leave a small sample to analyze Na 2 O content; repeat the above operation until Na in the molecular sieve 2 The O content reaches 2.5-5wt%, and the sample number obtained after drying is LYN-1.

Embodiment 3

[0085] The large-grain NaY molecular sieve LY-1 in Example 2 was replaced with LY-2, and the process of Example 2 was repeated to obtain a sample numbered LYN-2.

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Abstract

The invention discloses a hydrocracking method for producing low pour-point diesel. The method comprises the following steps: enabling a wax-containing diesel raw material to be in contact with a hydrocracking catalyst to perform a hydrocracking reaction, and carrying out separation on an obtained hydrocracking product to obtain heavy naphtha and the low pour-point diesel, wherein the hydrocracking catalyst is prepared from a hydrogenation active metal component and carriers; the carriers comprise a modified Y-type molecular sieve, a beta molecular sieve and aluminium oxide; the modified Y-type molecular sieve has the following properties that: an average diameter of crystal particles is 2.0 to 5.0mu m, relative crystallinity is 110% to 150%, a SiO2 / Al2O3 molar ratio is 10 to 50, a unit-cell parameter is 2.436 to 2.450nm, and a pore volume occupied by pores with a pore diameter of 2nm to 6nm is 60% to 90% of a total pore volume. The method is particularly suitable for processing the high pour-point wax-containing diesel under the medium-pressure condition, and has very high catalytic activity and diesel selectivity; moreover, the reduction extent of a pour point of a diesel fraction is large, and product properties of the diesel are improved.

Description

technical field [0001] The invention relates to a hydrocracking method, in particular to a hydrocracking method for maximum production of low-condensation diesel oil. Background technique [0002] Petroleum companies in the world mainly use hydrodesulfurization catalysts, hydrodearomatization catalysts and hydrodecondensation catalysts in the production of low-sulfur, low-aromatic, low-point clean diesel oil, and have developed a series of hydrogenation catalysts through various catalysts and process combinations. Modification and pour point depressing series technology. At present, the representative hydrodecondensation process technology is the MDDW single-stage hydrodecondensation (catalytic dewaxing) process technology developed by Exxon Mobil Company of the United States. The catalyst uses ZSM-5 as the carrier matrix to carry a small amount of metal Ni component; For the hydrogenation upgrading and pour point depressing process technology developed by Global Solution C...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G47/02C10G47/14C10G47/18C10G47/20B01J29/80
CPCB01J29/084B01J29/7007B01J29/80B01J2229/20B01J2229/40C10G47/02C10G47/14C10G47/18C10G47/20C10G2300/304C10G2300/4006C10G2300/4012C10G2300/4018C10G2400/02C10G2400/04
Inventor 刘昶曹均丰郝文月杜艳泽黄薇廖杰锋王凤来关明华
Owner CHINA PETROLEUM & CHEM CORP
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