Hydrocracking method for producing low pour-point diesel

A technology for hydrocracking and diesel oil, applied in chemical instruments and methods, hydrocarbon oil cracking, petroleum industry, etc., can solve the problems of increased production cost, complicated preparation process, and influence on the conversion of aromatics, and achieve good hydrothermal stability and preparation The effect of simple process and low production cost

Active Publication Date: 2017-11-14
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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  • Hydrocracking method for producing low pour-point diesel
  • Hydrocracking method for producing low pour-point diesel
  • Hydrocracking method for producing low pour-point diesel

Examples

Experimental program
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Embodiment 1

[0065] In this embodiment, the method of the present invention is used to prepare large-crystalline NaY molecular sieves.

[0066] Preparation of LY-1

[0067] (1) Preparation of gel: Under stirring conditions at a temperature of 25℃, slowly add 165mL water glass to 63mL of high-alkali sodium metaaluminate solution. After mixing well, add 42.5mL aluminum sulfate solution and 35.6mL low The alkali sodium metaaluminate solution is stirred at a constant temperature for 0.5 hours, and then the obtained synthetic solution is statically aged 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 constant temperature for 16 hours, after the crystallization is completed, quickly cool down with cold water and open The synthesized molecular sieve is taken out from the synthesis kettle, filtered, washed and dried to obtain the product LY-...

Embodiment 2

[0083] Firstly, the raw material large-grain NaY molecular sieve LY-1 is ammonium exchanged. The preparation concentration is 10 liters of 0.5mol / L ammonium nitrate aqueous solution. Weigh 2000 grams of small-crystalline NaY molecular sieve and dissolve it in 10 liters of prepared ammonium nitrate aqueous solution, stirring at 300 rpm, and stirring at a constant temperature of 90°C for 1 hour, then filter the molecular sieve and save a sample for analysis of Na 2 O content; repeat the above operation until Na in the molecular sieve 2 The O content reaches 2.5-5wt%, and the dried sample number is LYN-1.

Embodiment 3

[0085] The large-crystalline NaY molecular sieve LY-1 in Example 2 was replaced with LY-2, and the process of Example 2 was repeated, and the prepared sample was 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-pour point diesel. Background technique [0002] The world's petroleum companies mainly use hydrodesulfurization catalysts, hydrodearomatization catalysts, and hydrogenation depressurization catalysts in the production of low-sulfur, low-aromatic, and low-pour-point clean diesel. They have developed a series of hydrogenation through various catalysts and process combinations. A series of process technologies for upgrading and reducing condensation. At present, the representative hydrogenation depressurization process technology is the MDDW single-stage hydrogen depressurization (catalytic dewaxing) process technology developed by Exxon Mobil, USA. The catalyst adopts ZSM-5 as the carrier matrix and carries a small amount of metal Ni component; The pour point depressing process technology developed by Global Solution Company uses SDD800 and...

Claims

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Application Information

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Patent Type & Authority Applications(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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