A catalyst for f-t synthesis of middle distillate isomerization depressant and its special core-shell structure composite molecular sieve

A middle distillate and composite molecular sieve technology, which is applied in the field of core-shell structure composite molecular sieves, can solve the problems of molecular sieve skeleton destruction, hydrothermal stability decline, and complex process conditions, and achieve high isomerization selectivity and selectivity improvement.

Active Publication Date: 2018-07-24
SYNFUELS CHINA TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, using this method to treat molecular sieves will destroy the molecular sieve skeleton, resulting in a decrease in its hydrothermal stability, which will inevitably lead to a decrease in the yield of molecular sieves (J.Catal.319(2014)232), and the process needs to be treated by pickling The Al component deposited on the surface of the molecular sieve, the process conditions are very complicated

Method used

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  • A catalyst for f-t synthesis of middle distillate isomerization depressant and its special core-shell structure composite molecular sieve
  • A catalyst for f-t synthesis of middle distillate isomerization depressant and its special core-shell structure composite molecular sieve
  • A catalyst for f-t synthesis of middle distillate isomerization depressant and its special core-shell structure composite molecular sieve

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0072] Prepare aluminum sulfate aqueous solution, KOH aqueous solution, silica sol aqueous solution and 1-ethylpyridinium bromide (SDA) aqueous solution respectively, and mix them to obtain ZSM-22 molecular sieve sol, crystallize at 180°C for 24h, cool, Suction filtration, washing, drying at 80°C for 24 hours, and calcination at 500°C for 8 hours to obtain ZSM-22 molecular sieve. Among them, the amount of aluminum sulfate is Al 2 o 3 In terms of KOH, the amount of K 2 In terms of O, the amount of silica sol is SiO 2 In total, the feed ratio (molar ratio) is as follows:

[0073] SiO 2 / Al 2 o 3 =100,K 2 O / SiO 2 =0.6,H 2 O / SiO 2 =30, SDA / SiO 2 = 0.2.

[0074] Take 2.0g of potassium hydroxide and add it to 50g of deionized water, weigh 8.0g of dodecyltrimethylammonium bromide and add it to the potassium hydroxide solution. After it is completely dissolved, weigh 10.0g of ZSM-22 molecular sieve and add it to the solution middle. After fully stirring for half an hour,...

Embodiment 2

[0077] Add 12.0 g of the ZSM-22 molecular sieve in Example 1 into 0.801 L of aqueous sodium hydroxide solution (1.5 mol / L), then weigh 10.8 g of cetyltrimethylammonium bromide and add it to the mixed solution, and stir thoroughly For half an hour, put it into a stainless steel crystallization kettle, and pre-crystallize at a constant temperature of 100°C for 8h. After cooling down, the mixed solution was taken out, and 3.2 g of sulfuric acid was added to adjust the pH value to 8.0 under the condition of rapid stirring. After fully mixing, put it into a stainless steel crystallization kettle again, and crystallize at a constant temperature of 80°C for 48h under dynamic conditions. Then washing, drying and calcining to obtain the composite molecular sieve with core-shell structure.

[0078] Take some samples for X-ray powder diffraction measurement, Figure 5 It is the wide-angle XRD pattern of the sample, and the result shows that there is ZSM-22 molecular sieve in the obtain...

Embodiment 3

[0080] Add 12.0 g of the ZSM-22 molecular sieve in Example 1 into 0.801 L of aqueous sodium hydroxide solution (1.5 mol / L), then weigh 18.1 g of hexadecyltrimethylammonium bromide and add it to the mixed solution, and stir thoroughly For half an hour, put it into a stainless steel crystallization kettle, and pre-crystallize at a constant temperature of 70°C for 40h. After cooling down, the mixed solution was taken out, and 2.1 g of sulfuric acid was added to adjust the pH value to 11.5 under the condition of rapid stirring. After fully mixing, put it into a stainless steel crystallization kettle again, and crystallize at a constant temperature of 100°C for 24h under dynamic conditions. Then washing, drying and calcining to obtain the composite molecular sieve with core-shell structure.

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Abstract

The invention provides a catalyst used for isomeric pour point depression of middle distillate in F-T synthesis and a special core-shell structure composite molecular sieve of the catalyst. The composite molecular sieve takes a microporous ZSM-22 molecular sieve as a core and takes a mesoporous MCM-41 molecular sieve as a shell, wherein a relative proportion of the microporous ZSM-22 molecular sieve to the mesoporous MCM-41 molecular sieve is adjustable. A preparation method for the composite molecular sieve comprises the steps of: firstly, preparing the ZSM-22 molecular sieve; then, adding alkaline and an organic template agent into a mixed system containing the ZSM-22 molecular sieve for pre-crystallization; and regulating the pH value to 6.5-13.5, and carrying out crystallization treatment, thereby obtaining the composite molecular sieve. The catalyst, which is prepared by taking the core-shell structure ZSM-22 / MCM-41 composite molecular sieve as a carrier, is applied to hydroisomerization reaction of the middle distillate in F-T synthesis, and shows high isomeric selectivity; and especially, highly branched alkane selectivity is obviously improved. In the case that the conversion rate is 91.4%, the isomeric selectivity is kept to be higher than 90%, and the highly branched isomeric selectivity reaches 55.6%.

Description

technical field [0001] The invention relates to a catalyst for the isomerization depreciation of F-T synthetic middle distillate oil and its special core-shell structure composite molecular sieve. Background technique [0002] ZSM-22 molecular sieve has a strong acid center, good hydrothermal stability and unique shape selectivity, and exhibits excellent catalytic performance in long-chain alkane isomerization reactions. However, the active site of the molecular sieve at the orifice is highly acidic, resulting in a strong cracking activity based on the molecular sieve catalyst; and the one-dimensional ten-membered ring pore structure has a large diffusion limit, resulting in the isomerization of the single-branched paraffin as the main product. Mainly, while multi-branched alkanes have lower freezing point and better low temperature fluidity. Generally speaking, the introduction of mesopores into the microporous molecular sieve system can effectively improve the diffusion p...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/80C10G45/64
Inventor 任杰刘粟侥张怀科吕恩静杨勇李永旺
Owner SYNFUELS CHINA TECH CO LTD
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