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Two step process for the preparation of zeolite A by hydrothermal treatment of heulandite

Assignee: Lyondell Chemical Technology LP
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Filing: 1982-01-28
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Granted: 1983-08-30
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Expires: 2002-01-28
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Abstract

Abstract A two step hydrothermal process for the preparation of a sodium cation form of zeolite A from heulandite by (1) heat treating a mixture of heulandite in an aqueous solution of sodium hydroxide and filtering the mixture followed by (2) reacting the filtrate with at least 75 percent of a stoichiometric amount of sodium aluminate to form and precipitate zeolite A from solution and recovering zeolite A.

Inventors

  • 👤 Hsiang-ning Sun

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 09:58
CPC Classifications
C; C01; C01B; C01B33/00; C01B33/20; C01B33/26; C01B33/28; C01B33/2807; C01B33/2815; Y; Y10; Y10S; Y10S423/00; Y10S423/24

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 187 words
A hydrothermal process for the preparation of a sodium cation form of zeolite A from natural heulandite of the formula Ca 1/2.sub.x (AlO.sub.2).sub.x (SiO.sub.2).sub.y.ZH.sub.2 O wherein x=5 to 7, y/x=4.5 to 5.5 and z=1 to 30 which comprises the steps of: (a) heating at a temperature of from about 60° C. to 110° C. said natural heulandite in a 1 to 30 weight percent aqueous solution of sodium hydroxide to dissolve heulandite, the heulandite having a concentration of at least one gram heulandite per 100 cc of aqueous sodium hydroxide solution; (b) filtering the heulandite-sodium hydroxide solution to remove undissolved heulandite and elemental impurities and form a filtrate; (c) reacting the filtrate at a temperature of from about 60° C. to 110° C. in the presence of up to 15 weight percent of NaCl with at least 75 percent of a stoichiometric amount of sodium aluminate in an aqueous solution to precipitate and form zeolite A having a mean particle size of about 3 to 6 microns, said sodium aluminate having a concentration of from 1 to 16.5 weight percent in water; and recovering said zeolite A.
Claim 2
Dependent Claim 187 words
A hydrothermal process for the preparation of a sodium cation form of zeolite A from natural heulandite of the formula Ca 1/2.sub.x (AlO.sub.2).sub.x (SiO.sub.2).sub.y.ZH.sub.2 O wherein x=5 to 7, y/x=4.5 to 5.5 and z=1 to 30 which comprises the steps of: (a) heating at a temperature of from about 60° C. to 110° C. said natural heulandite in a 1 to 30 weight percent aqueous solution of sodium hydroxide to dissolve heulandite, the heulandite having a concentration of at least one gram heulandite per 100 cc of aqueous sodium hydroxide solution; (b) filtering the heulandite-sodium hydroxide solution to remove undissolved heulandite and elemental impurities and form a filtrate; (c) reacting the filtrate at a temperature of from about 60° C. to 110° C. in the presence of up to 15 weight percent of NaCl with at least 75 percent of a stoichiometric amount of sodium aluminate in an aqueous solution to precipitate and form zeolite A having a mean particle size of about 3 to 6 microns, said sodium aluminate having a concentration of from 1 to 16.5 weight percent in water; and recovering said zeolite A.
Claim 3
Dependent Claim 24 words
A process according to claim 1 wherein the aqueous sodium hydroxide solution is in the range of from 10 to 20 percent by weight.
Claim 4
Dependent Claim 25 words
A process according to claim 1 wherein the concentration of heulandite is from 4 to 16 g. per 100 cc of aqueous sodium hydroxide solution.
Claim 5
Dependent Claim 27 words
A process according to claim 1 wherein the temperature of heating in step (a) and reacting the filtrate in step (c) is from 90° to 100° C.
Claim 6
Dependent Claim 34 words
A process according to claim 1 wherein the heating in step (a) and reacting the filtrate in step (c) are carried out at a temperature of from 110° C. to 150° C. under pressure.
Claim 7
Dependent Claim 29 words
The process according to claim 1 wherein the heating in step (a) and reacting the filtrate in step (c) are carried out for from 15 minutes to 4 hours.
Claim 8
Dependent Claim 15 words
The process of claim 6 wherein the time is from 15 minutes to 1 hour.
Claim 9
Dependent Claim 18 words
A process according to claim 1 wherein a stoichiometric amount of sodium aluminate in aqueous solution is employed.
Claim 10
Dependent Claim 21 words
A process according to claim 1 wherein said sodium aluminate concentration in water is from 4 to 15 percent by weight.
Claim 11
Dependent Claim 21 words
A process according to claim 1 wherein the NaCl based on the aqueous sodium hydroxide solution is added in step (a).
Claim 12
Dependent Claim 21 words
A process according to claim 1 wherein the NaCl based on the sodium aluminate aqueous solution is added in step (c).
Claim 13
Dependent Claim 27 words
A process according to claim 1 wherein from 0 to 30 weight percent sodium hydroxide based on the aqueous sodium aluminate solution is added in step (c).

References Cited (Backward Citations)

CA667751A Cited
US3733390A Cited
US4310496A Cited
US4247524A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-08-29 1987-02-28 1987-08-30 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-08-29 1991-02-28 1991-08-30 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-08-29 1995-02-28 1995-08-30 $7700.00 Window Closed / Lapsed

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