VERFAHREN ZUR HERSTELLUNG VON ZEOLITH Y
1437869 Zeolite Y UNION CARBIDE CORP 7 May 1974 [8 May 1973] 19983/74 Heading C1A Zeolite Y is prepared by (a) providing in a sealable reaction vessel a homogeneous aqueous aluminosilicate reaction mixture in which the source of silica is solid reactive amorphous silica, the reaction mixture having...
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Format | Patent |
Language | German |
Published |
19.12.1974
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Abstract | 1437869 Zeolite Y UNION CARBIDE CORP 7 May 1974 [8 May 1973] 19983/74 Heading C1A Zeolite Y is prepared by (a) providing in a sealable reaction vessel a homogeneous aqueous aluminosilicate reaction mixture in which the source of silica is solid reactive amorphous silica, the reaction mixture having the following composition Na 2 O/SiO 2 0À30-0À36, SiO 2 /Al 2 O 3 8À0-11, H 2 O/Na 2 O 16-35 (oxide-mole ratios), (b) maintaining the reaction mixture at 95- 160 F. for 6-15 hours (optionally with agitation), (c) injecting steam into the reaction mixture to raise the temperature to 240-300 F. while not increasing the water content by not more than 15% by weight, (d) maintaining the reaction mixture under autogenous pressure for 4-20 hours at 240-300 F. and (e) rapidly decreasing the pressure from autogenous to atmospheric to obtain a temperature decrease of at least 35 F. in a period not exceeding 10 minutes. The process may include an additional step of filtering and washing the reaction mass solid to recover Zoelite Y crystals. |
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AbstractList | 1437869 Zeolite Y UNION CARBIDE CORP 7 May 1974 [8 May 1973] 19983/74 Heading C1A Zeolite Y is prepared by (a) providing in a sealable reaction vessel a homogeneous aqueous aluminosilicate reaction mixture in which the source of silica is solid reactive amorphous silica, the reaction mixture having the following composition Na 2 O/SiO 2 0À30-0À36, SiO 2 /Al 2 O 3 8À0-11, H 2 O/Na 2 O 16-35 (oxide-mole ratios), (b) maintaining the reaction mixture at 95- 160 F. for 6-15 hours (optionally with agitation), (c) injecting steam into the reaction mixture to raise the temperature to 240-300 F. while not increasing the water content by not more than 15% by weight, (d) maintaining the reaction mixture under autogenous pressure for 4-20 hours at 240-300 F. and (e) rapidly decreasing the pressure from autogenous to atmospheric to obtain a temperature decrease of at least 35 F. in a period not exceeding 10 minutes. The process may include an additional step of filtering and washing the reaction mass solid to recover Zoelite Y crystals. |
Author | WEBER, WILLIS WILMER, SOUTH SALEM, N.Y. (V.ST.A.) |
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Notes | Application Number: DE19742421884 |
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RelatedCompanies | UNION CARBIDE CORP., NEW YORK, N.Y. (V.ST.A.) |
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Snippet | 1437869 Zeolite Y UNION CARBIDE CORP 7 May 1974 [8 May 1973] 19983/74 Heading C1A Zeolite Y is prepared by (a) providing in a sealable reaction vessel a... |
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Title | VERFAHREN ZUR HERSTELLUNG VON ZEOLITH Y |
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