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Preparation method for isodewaxing catalyst

A technology of isomerization dewaxing and catalyst, which is applied in molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., to achieve the effects of high yield, low pour point and high metal dispersion

Active Publication Date: 2016-01-06
CHINA NAT OFFSHORE OIL CORP +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] How to improve the selectivity of the isomerization dewaxing catalyst, that is, the base oil yield, has always been a research hotspot. Although the above patents use different methods to improve the selectivity of the catalyst as much as possible, there is still room for further improvement.

Method used

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  • Preparation method for isodewaxing catalyst

Examples

Experimental program
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Effect test

Embodiment 1

[0026] (1) Synthesis of ZSM-22 molecular sieve

[0027] The ZSM-22 molecular sieve was synthesized according to the patent US4556477. ① 28.6g silica sol (30wt% SiO 2 ) and 29.8g deionized water are mixed evenly; ② 1g aluminum sulfate (17.2wt%Al 2 o 3 ), 2.3g of potassium hydroxide and 52.3g of deionized water were mixed evenly; ③Mix and stir the ① and ② solutions for 15min, then add 5g of hexamethylenediamine into the mixed solution and stir; ④Put the ③ solution into a stirring In a high-pressure reactor, heat to 160°C, stir and react for 72h; ⑤After washing and filtering, the filter cake is dried at 110°C for 10h to obtain SiO 2 / Al 2 o 3 ZSM-22 molecular sieve raw powder with a molar ratio of about 60.

[0028] (2) Molecular sieve modification:

[0029] ①Calcinate ZSM-22 raw powder at 600℃ for 6h; ②Use 0.3mol / L NH 4 NO 3 The aqueous solution performs ion exchange on the molecular sieve. The exchange conditions are: the mass ratio of solid to liquid is 1:10, the exc...

Embodiment 2

[0031] (1) Synthesis of ZSM-23

[0032] The synthesis of ZSM-23 is according to the disclosed method of U.S. Patent No. 4,076,842: 1. 3.3g sodium metaaluminate (43.1wt%Al 2 o 3 , 33.1 wt% Na 2 O and 24.7 wt% H 2 O), 30g deionized water and 0.34gNaOH (50wt% aqueous solution) are mixed, stirred evenly, then add 18.2g pyrrolidine and continue to stir; ② 164.8g silica sol (30% SiO 2 ,70%H 2 0) add the above solution and stir until a gel is formed; ③ put the above gel into an autoclave to heat and stir, and continuously crystallize at 180° C. for 7 days; ④ wash and filter the product until the filtrate is neutral, Dry the filter cake at 110°C for about 16 hours to obtain SiO 2 / Al 2 o 3 ZSM-23 molecular sieve raw powder with a molar ratio of about 60.

[0033] (2) Molecular sieve modification method According to the method of Example 1, H-ZSM-23 was obtained.

Embodiment 3

[0035] Synthesis of SAPO-11 molecular sieve is carried out according to patent CN103043683B: ① 2g hexadecyl triethoxy organosilicon quaternary ammonium salt is dissolved in 18g ethanol; ② 23.1g phosphoric acid (AR, 85%) is mixed with 72.0g deionized water in Mix well in a water bath at 38°C, add 15.2g of pseudoboehmite (Shandong aluminum powder, aluminum oxide content 67%), stir in a water bath at 38°C for 0.5h to obtain aluminum phosphate sol; then slowly add 11.2g of Propylamine (DPA, AR, 99%) continued to stir for 0.5h; added 6.3g tetraethyl orthosilicate (AR, 99%), continued to stir for 0.5h, then added 20g of ① solution, continued to stir for 2h; ④ put the above solution into high pressure In the reaction kettle, aged at 130°C for 2h, then heated to 190°C, and crystallized for 36h; ⑤The obtained crystals were washed and filtered and then dried at 120°C for 12h to obtain the original SAPO-11 molecular sieve powder; ⑥The original powder was heated at 600 Calcined at ℃ for 6...

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Abstract

The invention discloses a preparation method for an isodewaxing catalyst. According to the method, a certain amount of alkaline-earth metal soluble salt solution is added during molding of a catalyst carrier to modify the carrier; in the step of loading active metal components, the solvothermal-ion exchange method is adopted, wherein water is replaced with solvent, and the active components are loaded to the catalyst carrier in the mode of ion exchange under certain temperature and pressure conditions. The invention further provides the isodewaxing catalyst prepared through the method. The catalyst is used for isodewaxing lubricating oil distillate and producing lubricant base oil with a low pour point and a high viscosity index, and has the advantages that the acidity of the catalyst is moderate, metal dispersity is high, isodewaxing reactivity and selectivity are high, and the lubricant base oil is low in pour point and high in yield.

Description

technical field [0001] The invention relates to the field of catalyst preparation, in particular to a heterogeneous dewaxing catalyst for producing lubricating oil base oil and a preparation method thereof. Background technique [0002] Lubricating oil fractions, especially paraffin-based lubricating oil fractions, contain a large amount of n-paraffins with long carbon chains. Normal alkanes have a high melting point and are solid at room temperature, which seriously affects the low-temperature fluidity of lubricating oils. Solvent dewaxing, catalytic dewaxing and isomerization dewaxing are used to improve the low temperature fluidity of lubricating oils. [0003] Solvent dewaxing is a traditional method, which uses the solubility of solvents to remove wax, which has the disadvantages of environmental pollution and high operating costs; catalytic dewaxing is to crack wax molecules into small molecular hydrocarbons to improve the low-temperature fluidity of oil products. The...

Claims

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Application Information

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IPC IPC(8): B01J29/74B01J29/85C10G45/12C10G45/64C10M177/00C10M101/02
Inventor 孙国方于海斌李孝国费亚南赵甲臧甲忠高鹏刘有鹏郑修新李佳隋芝宇张永惠
Owner CHINA NAT OFFSHORE OIL CORP