Catalyst for poly-alpha-olefin synthetic oil and preparation method for catalyst

A technology of olefin synthesis oil and catalyst, which is applied in the direction of molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., to achieve the effects of good quality, easy process operation, and high yield

Active Publication Date: 2017-06-23
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, there are few reports on catalysts for the direct polym

Method used

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  • Catalyst for poly-alpha-olefin synthetic oil and preparation method for catalyst

Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0036] Example 1

[0037] Put 8g silica (pore volume 0.50cm 3 / g, average pore diameter is 2.0nm, specific surface area is 158m 2 / g) immersed in vanadium nitrate aqueous solution (V loading is 0.20wt%), continuously stirred and immersed in a water bath at 25°C for 30 minutes, filtered, and vacuum dried at 100°C for 6 hours; put the silica support impregnated with vanadium nitrate in a muffle For roasting in the furnace, the temperature is first raised to 120°C for 2 hours, then to 350°C for 1 hour, then to 450°C for 6 hours, and finally cooled down naturally under nitrogen. The obtained sample was again immersed in a toluene solution of aluminum trichloride (Al loading amount was 12.00 wt%), continuously stirred and immersed for 2 hours at room temperature, and vacuum dried at 100° C. for 6 hours to obtain the catalyst and save it for use.

Example Embodiment

[0038] Example 2

[0039] Put 8g silica (pore volume 0.58cm 3 / g, the average pore diameter is 12.5nm, the specific surface area is 100m 2 / g) immersed in vanadyl oxalate aqueous solution (V loading is 0.58wt%), continuously stirred and dipped in a 45℃ water bath for 50 min, filtered, and vacuum dried at 100℃ for 6 h; put the silica carrier impregnated with vanadyl oxalate on For roasting in the muffle furnace, the temperature is first raised to 120°C for 2 hours, then to 350°C for 1 hour, then to 450°C for 6 hours, and finally cooled down naturally under nitrogen. The obtained sample was again immersed in an isopropanol solution of titanium tetrachloride (Ti loading amount was 10.68wt%), continuously stirred and immersed for 2 hours at room temperature, and vacuum dried at 100°C for 6 hours. The obtained catalyst was stored for later use.

Example Embodiment

[0040] Example 3

[0041] 10g aluminum oxide (γ-alumina, pore volume of 1.34cm 3 / g, the average pore diameter is 20nm, the specific surface area is 220m 2 / g) immersed in chromium acetate aqueous solution (Cr loading amount is 12.00wt%), continuously stirred and immersed in a water bath at 25°C for 60 minutes, filtered, and vacuum dried at 100°C for 6 hours; put the aluminum oxide carrier impregnated with chromium acetate on the horse For roasting in the Furnace, the temperature is first raised to 120°C, constant temperature for 2h, then to 350°C, constant temperature for 1h, then to 550°C, constant temperature for 6h, and finally cooled to 200-300°C under nitrogen, with reducing The gas CO, lasts for 1-3h, reduces the chromium oxide contained in it to low-priced chromium oxide. The obtained sample was again immersed in an isopropanol solution of titanium tetrachloride (Ti loading amount was 0.10 wt%), continuously stirred and immersed for 4 hours at room temperature, and vacuum...

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Abstract

The invention relates to a catalyst for poly-alpha-olefin synthetic oil. The catalyst comprises the following ingredients: a support and active ingredients, wherein the support is a porous inorganic support, and the active ingredients comprise a metal oxide and a Lewis acid type metal salt. The invention further provides a preparation method for the catalyst. The preparation method comprises the steps: dissolving a metal salt of the metal oxide, which serves as a raw material, in deionized water, dipping the support with the obtained metal salt solution, and then, carrying out drying, so as to obtain a metal salt loaded support; roasting the metal salt loaded support in a muffle furnace, so as to obtain a metal oxide loaded catalyst matrix; and then, adding the metal oxide loaded catalyst matrix into an organic solvent containing the Lewis acid type metal salt for loading, thereby obtaining a loaded dual-active-center catalyst.

Description

technical field [0001] The invention relates to a supported double-active center catalyst for preparing high-viscosity index polyalpha-olefin synthetic oil base oil and a preparation method thereof. Background technique [0002] Poly-α-olefin (PAO) synthetic oil is currently the best synthetic lubricating base oil, with high viscosity index, low volatility, low fluidity, good shear performance and excellent high temperature oxidation resistance; and traditional Compared with mineral lubricating oil base oils (Ⅰ, Ⅱ, Ⅲ base oils), PAO has the characteristics of small evaporation loss, good stability, wide temperature range, good compatibility with common materials and non-toxicity. It is not only used in automobiles, It is widely used in civil industries such as industry, and it is also the main source of high-grade lubricating oil base oil used in aviation, aerospace, military and other industries. [0003] PAO is generally composed of C 6 -C 20 A class of oligomers with b...

Claims

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Application Information

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IPC IPC(8): B01J27/135B01J27/125B01J27/128B01J29/03C10G50/02
CPCB01J27/125B01J27/128B01J27/135B01J29/0341B01J2229/183C10G50/02C10G2300/1088C10G2300/302C10G2300/70
Inventor 刘通王力搏王斯晗徐显明褚洪岭高立平王桂芝曹媛媛王亚丽王秀绘白玉洁于部伟马克存赵仲阳孙恩浩蒋岩闫义斌朱丽娜姜宁贾鹏飞韩雪梅黄付玲韩云光林如海
Owner PETROCHINA CO LTD
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