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SAPO-11 molecular sieve, manufacturing method thereof, and application thereof in hydrocarbon isomerization

A technology of SAPO-11 and molecular sieve, which is applied to molecular sieve catalysts, including molecular sieve catalysts, molecular sieves and base-exchanged phosphates, can solve problems such as environmental impact and increased production costs, and achieve high double-branched isomerization selectivity and low Cracking selectivity, effect of increasing gasoline octane number

Active Publication Date: 2018-02-16
CHINA UNIV OF PETROLEUM (BEIJING)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] In summary, it can be seen that in the prior art, additional templates need to be added in the process of preparing the carrier SAPO-11 of hydrocarbon isomerization catalysts, and most of the templates are organic templates, and the use of templates will cause certain damage to the environment. Affect and increase the preparation cost

Method used

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  • SAPO-11 molecular sieve, manufacturing method thereof, and application thereof in hydrocarbon isomerization
  • SAPO-11 molecular sieve, manufacturing method thereof, and application thereof in hydrocarbon isomerization
  • SAPO-11 molecular sieve, manufacturing method thereof, and application thereof in hydrocarbon isomerization

Examples

Experimental program
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Embodiment 1

[0050] Dissolve 6.25g of aluminum isopropoxide in 51.70g of ethylene glycol, and stir at 25°C for 1 hour to obtain solution A;

[0051] 7.62g di-n-propylamine and 6.22g H 3 PO 4 Add to the above solution A, and stir at 25°C for 2 hours to obtain solution B;

[0052] Add 1.28g of ethyl orthosilicate to the above solution B, and stir at 25°C for 1.5h to obtain solution C;

[0053] Transfer the above solution C to 100 ml supercritical CO 2 The reaction kettle was sealed, and CO was introduced into the reaction kettle at 25°C. 2 , so that the pressure in the reactor reaches 62.07bar;

[0054] Supercritical CO 2 The temperature of the reaction kettle was raised to 200°C, the self-generated pressure reached 124.14bar, and the constant temperature crystallized for 144h;

[0055] Supercritical CO 2 Cool the reaction kettle to 25°C, centrifuge the product, dry at 120°C for 12 hours, and roast in an air atmosphere at 600°C for 6 hours to obtain SAPO-11 molecular sieve powder, whi...

Embodiment 2

[0066] Dissolve 7.50g of aluminum isopropoxide in 51.70g of ethylene glycol, and stir at 25°C for 1 hour to obtain solution A;

[0067] 7.32g di-n-propylamine and 5.98g H 3 PO 4 Add to the above solution A, and stir at 25°C for 2 hours to obtain solution B;

[0068] Add 1.22g of tetraethyl orthosilicate to the above solution B, and stir at 25°C for 1.5h to obtain solution C;

[0069] Transfer the above solution C to a tank with 100 ml supercritical CO 2 The reaction kettle was sealed, and CO was introduced into the reaction kettle at 25°C. 2 , so that the pressure in the reactor reaches 50.00bar;

[0070] Supercritical CO 2 The temperature of the reaction kettle was raised to 200°C, the self-generated pressure reached 90.25bar, and the constant temperature crystallized for 144h;

[0071] Supercritical CO 2 Cool the reaction kettle to 25°C, centrifuge the product, dry at 120°C for 12 hours, and roast in an air atmosphere at 600°C for 6 hours to obtain SAPO-11 molecular s...

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Abstract

The invention provides an SAPO-11 molecular sieve, a manufacturing method thereof, and an application thereof in hydrocarbon isomerization. The manufacturing method comprises the following steps: dissolving an aluminum source in glycol, stirring to obtain a solution A; adding a structure-directing agent and a phosphor source into the solution A, stirring to obtain a solution B; adding a silicon source into the solution B, stirring to obtain a solution C; transferring the solution C to an supercritical CO2 reactor, introducing CO2 into the reactor to raise the pressure; heating the reactor to areaction temperature, carrying out crystallization; after crystallization, reducing the temperature of the supercritical CO2 reactor, taking out the solution in the reactor, separating the product, drying, and burning the product to obtain SAPO-11. The method does not need any template, and can prepare SAPO-11 having an advantage of small crystal grain size and a meso-structure. The molecular sieved is moulded, a metal component is loaded on the molecular sieve, and then the molecular sieve is dried and burned to obtain a hydrocarbon isomerization catalyst, which has higher double branch chain isomerization selectivity and lower cracking selectivity and can be applied to hydrocarbon isomerization reactions.

Description

technical field [0001] The invention relates to a molecular sieve and its preparation method and application, in particular to a SAPO-11 molecular sieve, its preparation method and the application of the SAPO-11 molecular sieve as a hydrocarbon isomerization catalyst carrier, belonging to the field of catalysts. Background technique [0002] Hydrocarbon hydroisomerization is an important technology in the petroleum refining process. The branched isomers produced by hydroisomerization can significantly reduce the pour point of lubricating oil, improve the viscosity-temperature properties of diesel oil, and increase the octane number of gasoline. The Pt / SAPO-11 catalyst has suitable acid sites and metal active sites, and has excellent catalytic activity for hydrocarbon hydroisomerization. The orifice of the microporous channel in the SAPO-11 molecular sieve is an elliptical ten-membered ring structure of 0.39nm×0.63nm, and its length is used as a carrier for hydrocarbon isome...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B39/54C01B37/08B01J29/85C07C5/13C07C9/16
CPCB01J29/85C01B37/08C01B39/54C01P2004/04C01P2006/12C07C5/13C07C9/16B01J23/42B01J23/883B01J37/0018B01J37/0201B01J37/0236B01J37/08B01J2203/068C07C2529/85Y02P20/54B01J37/04C07C2523/42
Inventor 范煜韩善雷文成龙王世华
Owner CHINA UNIV OF PETROLEUM (BEIJING)