Carrier and catalyst for selectively synthesizing kerosene fraction from syngas, and method for preparing the same

US10286389B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10286389-B2
Application numberUS-201715839835-A
CountryUS
Kind codeB2
Filing dateDec 12, 2017
Priority dateJun 16, 2015
Publication dateMay 14, 2019
Grant dateMay 14, 2019

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  1. Title

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  2. Abstract

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  4. Key dates

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  5. First independent claim

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Abstract

Official abstract text for this publication.

A carrier for selectively synthesizing kerosene fraction from syngas, the carrier including the following components in parts by weight: 5-50 parts of mesoporous zirconia (ZrO 2 ), 10-55 parts of a silicoaluminophosphate (SAPO) molecular sieve, 5-50 parts of modified mesoporous molecular sieve Al-SBA-16, 1-3 parts of sesbania gum powder, and 10-70 parts of alumina A catalyst includes a soluble cobalt salt and the aforesaid carrier. The soluble cobalt salt is loaded on the surface of the carrier.

First claim

Opening claim text (preview).

The invention claimed is: 1. A carrier, comprising the following components in parts by weight: 5-50 parts of mesoporous zirconia (ZrO 2 ), 10-55 parts of a silicoaluminophosphate (SAPO) molecular sieve, 5-50 parts of modified mesoporous molecular sieve Al-SBA-16, 1-3 parts of sesbania gum powder, and 10-70 parts of alumina. 2. The carrier of claim 1 , comprising the following components in parts by weight: 10-30 parts of the mesoporous zirconia, 25-45 parts of the silicoaluminophosphate molecular sieve, 10-30 parts of the modified Al-SBA-16, 1-3 parts of the sesbania gum powder, and 30-55 parts of the alumina. 3. The carrier of claim 2 , comprising the following components in parts by weight: 20 parts of the mesoporous zirconia, 30 parts of the silicoaluminophosphate molecular sieve, 25 parts of the modified Al-SBA-16, 1 part of the sesbania gum powder, and 30 parts of the alumina. 4. The carrier of claim 1 , wherein the modified Al-SBA-16 comprises SBA-16 and aluminum triethoxide (Al(OC 2 H 7 ) 3 ), in which a weight ratio of SBA-16 to aluminum triethoxide is 1:3.0-4.5. 5. The carrier of claim 3 , wherein the modified Al-SBA-16 comprises SBA-16 and aluminum triethoxide (Al(OC 2 H 7 ) 3 ), in which a weight ratio of SBA-16 to aluminum triethoxide is 1:3.0-4.5. 6. The carrier of claim 1 , wherein a molar ratio n of silicon to aluminum in the modified Al-SBA-16 is between 5 and 55, a Brönsted acid (B acid) content thereof is 39-92 μmol·g −1 , a Lewis acid (L acid) content thereof is 71-105 μmol·g −1 , and a Na 2 O content thereof is ≤0.1 wt. %. 7. The carrier of claim 3 , wherein a molar ratio n of silicon to aluminum in the modified Al-SBA-16 is between 5 and 55, a Brönsted acid (B acid) content thereof is 39-92 μmol·g −1 , a Lewis acid (L acid) content thereof is 71-105 μmol·g −1 , and a Na 2 O content thereof is ≤0.1 wt. %. 8. The carrier of claim 6 , wherein the molar ratio n of silicon to aluminum in the modified Al-SBA-16 is between 10 and 55, a specific surface area is 550-930 m 2 ·g −1 , an average pore size is 4.0-7.5 nm, and a total pore volume is 0.45-0.70 cm 3 ·g −1 . 9. The carrier of claim 7 , wherein the molar ratio n of silicon to aluminum in the modified Al-SBA-16 is between 10 and 55, a specific surface area is 550-930 m 2 ·g −1 , an average pore size is 4.0-7.5 nm, and a total pore volume is 0.45-0.70 cm 3 ·g −1 . 10. The carrier of claim 1 , wherein the modified mesoporous molecular sieve Al-SBA-16 is prepared as follows: 1) weighing SBA-16 and aluminum triethoxide according to an aforesaid weight ratio, and dividing the aluminum triethoxide into two equal portions for use; 2) adding SBA-16 to n-hexane, and uniformly stirring at room temperature, to obtain a mixed solution; adding one portion of the aluminum triethoxide to n-hexane, and stirring at room temperature until the aluminum triethoxide is dissolved; and adding the aluminum triethoxide dissolved in the n-hexane to the mixed solution, and stirring overnight at room temperature, to obtain a sample solution; 3) transferring the sample solution obtained in 2) to a Buchner funnel, washing with n-hexane, and suctioning; and repeating the washing and suctioning operations 2 to 4 times, to obtain a primary filter cake; 4) adding the primary filter cake to n-hexane, and uniformly stiffing at room temperature; adding another portion of the aluminum triethoxide; stirring overnight at room temperature, transferring to a Buchner funnel, washing with n-hexane, and suctioning; and repeating the washing and suctioning operations 2 to 4 times, to obtain a secondary filter cake; and 5) baking the secondary filter cake at 500-650° C. for 6-10 h, to obtain modified Al-SBA-16. 11. The carrier of claim 1 , wherein the mesoporous zirconia has a specific surface area of 190-350 m 2 ·g −1 , an average pore size of 5.0-8.5 nm, and a total pore volume of 0.40-0.55 cm 3 ·g −1 . 12. The carrier of claim 1 , wherein the silicoaluminophosphate molecular sieve has a total acid content of 0.1-0.35 mmol NH 3 ·g −1 ; a molar ratio of silicon to aluminum of 0-1.0; a specific surface area of ≥150 m 2 ·g −1 , a Na 2 O content of ≤0.2 wt. %, and a total pore volume of 0.10-0.30 cm 3 ·g −1 . 13. The carrier of claim 12 , wherein the silicoaluminophosphate molecular sieve has a molar ratio of silicon to aluminum of 0.21-0.38, a specific surface area of ≥180 m 2 ·g −1 , a Na 2 O content of ≤0.2 wt. %, and a total pore volume of 0.10-0.30 cm 3 ·g −1 ; or the silicoaluminophosphate molecular sieve has a molar ratio of silicon to aluminum of 0-1.0, a specific surface area of ≥150 m 2 ·g −1 , a Na 2 O content of ≤0.2 wt. %, and a total pore volume of 0.13-0.26 cm 3 ·g −1 . 14. A method for preparing a carrier, the method comprising: 1) separately weighing out SBA-16 and aluminum triethoxide according to a weight ratio 1:3.0-4.5, and dividing the aluminum triethoxide into two equal portions; 2) adding the SBA-16 to n-hexane, and uniformly stiffing at room temperature, to obtain a mixed solution; adding one portion of the aluminum triethoxide to n-hexane, and stiffing at room temperature until the aluminum triethoxide is dissolved; and adding the aluminum triethoxide dissolved in the n-hexane to the mixed solution, and stiffing overnight at room temperature, to obtain a sample solution; 3) transferring the sample solution obtained in 2) to a Buchner funnel, washing with n-hexane, and suctioning; and repeating the washing and suctioning operations 2 to 4 times, to obtain a primary filter cake; 4) adding the primary filter cake to n-hexane, and stiffing at room temperature; adding another portion of the aluminum triethoxide; stirring overnight at room temperature, transferring to a Buchner funnel, washing with n-hexane, and suctioning; and repeating the washing and suctioning operations 2 to 4 times, to obtain a secondary filter cake; 5) baking the secondary filter cake at 500-650° C. for 6-10 h, to obtain modified Al-SBA-16 for use; 6) uniformly kneading microporous alumina with a dilute nitric acid solution at a weight ratio of 1:0.5-1.5, to prepare a viscous paste for use, in which the concentration of the dilute nitric acid solution is 5-20 wt. %; and 7) weighing, in parts by weight, 5-50 parts of mesoporous zirconia, 10-55 parts of the silicoaluminophosphate molecular sieve, 5-50 parts of modified Al-SBA-16, 1-3 parts of sesbania gum powder and 10-70 parts of the viscous paste based on alumina; and uniformly mixing aforesaid components, rolling, extrusion molding, drying for 6-12 h at 90-120° C., then baking for 4-10 h in air at 500-600° C., and cooling to room temperature to obtain the carrier. 15. The method of claim 14 , wherein the carrier is in the shape of a cylindrical strip, a clover or a four-leaf clover; the carrier in the shape of a cylindrical strip has a particle size of 1.2-1.6 mm, and a length of 5-10 mm; and the carrier in the shape of a clover or a four-leaf clover has a distance between two leaves of 1.1-1.8 mm, and a length of 5-10 mm. 16. A catalyst, comprising a soluble cobalt salt and a carrier of claim 1 , the soluble cobalt salt being loaded on a surface of the carrier. 17. The catalyst of claim 16 , wherein the soluble cobalt salt accounts for 5-20 wt. % of the catalyst. 18. The catalyst of claim 16 , wherein the soluble cobalt salt is cobalt nitrate, cobalt acetate or carbonyl cobalt. 19. The catalyst of claim 17 , wherein the soluble cobalt salt is cobalt nitrate, cobalt acetate or carbonyl cobalt. 20. A method for preparing the catalyst of claim 16 , compris

Assignees

Inventors

Classifications

  • the catalyst containing other metals or compounds thereof · CPC title

  • Diesel oil · CPC title

  • Zirconium or hafnium; Oxides or hydroxides thereof · CPC title

  • Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon · CPC title

  • B01J29/85Primary

    Silicoaluminophosphates [SAPO compounds] · CPC title

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What does patent US10286389B2 cover?
A carrier for selectively synthesizing kerosene fraction from syngas, the carrier including the following components in parts by weight: 5-50 parts of mesoporous zirconia (ZrO 2 ), 10-55 parts of a silicoaluminophosphate (SAPO) molecular sieve, 5-50 parts of modified mesoporous molecular sieve Al-SBA-16, 1-3 parts of sesbania gum powder, and 10-70 parts of alumina A catalyst includes a soluble …
Who is the assignee on this patent?
Wuhan Kaidi Eng Tech Res Inst
What technology area does this patent fall under?
Primary CPC classification B01J29/85. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue May 14 2019 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).