InventorsRobert Scott Smith, Johannes Petrus Verduijn, deceased, Jannetje Maatje van den Berge, executrix, Thomas H. Colle, Gary David Mohr, Gotz Burgfels, Josef Schonlinner
Large crystal zeolites are prepared by heating a zeolite synthesis mixture under agitation to a temperature equal to or less than the effective nucleation temperature of the zeolite synthesis mixture and thereafter the zeolite synthesis mixture is heated without agitation to a temperature equal to or greater than the effective nucleation temperature of the zeolite synthesis mixture.
Drawings
Claims26
A process for preparing large crystal zeolite comprising:
(a) heating an aqueous synthesis mixture comprising sources of trivalent metal oxide, silica, alkali metal cations, optionally from 0 to about 10 weight percent of seeds of zeolite, and optionally a directing agent under agitation to a temperature equal to or less than the effective nucleation temperature of said aqueous reaction mixture;
and,
(b) heating said aqueous synthesis mixture in the absence of agitation at a temperature equal to or greater than the effective nucleation temperature of said aqueous reaction mixture.
A process of preparing MFI or MEL structure-type large zeolite crystals comprising the steps of:
(a) forming an aqueous reaction mixture comprising sources of trivalent metal oxide, silica, alkali metal cations, optionally from 0 to about 10 weight percent seed crystals;
and, optionally a directing agent;
(b) heating the aqueous reaction mixture under agitation to a temperature no greater than the effective nucleation temperature of said aqueous reaction mixture;
and,
(c) heating the aqueous reaction mixture of step (b) in the absence of agitation to a temperature equal to or greater than the effective nucleation temperature of said aqueous reaction mixture and for sufficient time to result in the production of large zeolite crystals.
17 Oct 2017Estimated · howhide20 years from earliest known nonprovisional domestic filing. Maintenance-fee lapses, terminal disclaimers and statutory extensions have not been checked. The continuity chain may be incomplete; this is not an enforceability determination. Patent term adjustment is unavailable; no adjustment was added.
Chemistry of inorganic compounds: mel, e.g. zsm-11
Life of this patent
Term ended 17 Oct 2017 (estimated)
Priority17 Oct 1997
Granted28 Sep 1999
Term ended17 Oct 2017
Priority17 Oct 1997
Granted28 Sep 1999
Term ended17 Oct 2017
Application filedUS 08/954,341
GrantedUS 5,958,366 A
Term endedEstimated
USPTO file history isn’t available for this patent, so only indexed dates are shown.
Description4,493 words
Summary3,754 words
#This invention relates to a method of preparing crystalline zeolites wherein the crystalline zeolites are crystallized in the form of large crystals.
#Crystalline microporous molecular sieves, both natural and synthetic, such as zeolites, have been demonstrated to have catalytic properties for various types of hydrocarbon conversion processes. In addition, the crystalline microporous molecular sieves have been used as adsorbents and catalyst carriers for various types of hydrocarbon conversion processes, and other applications. These molecular sieves are ordered, porous, crystalline material having a definite crystalline structure as determined by x-ray diffraction, within which there are a large number of smaller cavities which may be interconnected by a number of still smaller channels or pores. The dimensions of these channels or pores are such as to allow adsorption of molecules with certain dimensions while rejecting those with larger dimensions. The interstitial spaces or channels formed by the crystalline network enable molecular sieves, such as crystalline aluminosilicates, to be used as molecular sieves in separation processes and catalysts and catalyst supports in a wide variety of hydrocarbon conversion processes.
#Zeolites are comprised of a lattice of silica and optionally alumina combined with exchangeable cations such as alkali or alkaline earth metal ions. Although the term "zeolites" includes materials containing silica and optionally alumina, it is recognized that the silica and alumina portions may be replaced in whole or in part with other oxides. For example, germanium oxide, tin oxide, phosphorous oxide, and mixtures thereof can replace the silica portion. Boron oxide, iron oxide, titanium oxide, gallium oxide, indium oxide, and mixtures thereof can replace the alumina portion. Accordingly, the terms "zeolite", "zeolites" and "zeolite material", as used herein, shall mean not only molecular sieves containing silicon and, optionally, aluminum atoms in the crystalline lattice structure thereof, but also molecular sieves which contain suitable replacement atoms for such silicon and aluminum, such as silicoaluminophosphates (SAPO) and aluminophosphates (ALPO). The term "aluminosilicate zeolite", as used herein, shall mean zeolites consisting essentially of silicon and aluminum atoms in the crystalline lattice structure thereof.
Detailed description739 words
#The following examples exemplify the process of the present invention.
#A sodium aluminate solution was prepared by dissolving alumina hydrate (201 parts by weight, 65% Al.sub.2 O.sub.3 content) in a caustic solution comprising NaOH (369.1 parts by weight) and water (825 parts by weight) at 100.degree. C. The solution was cooled and then added with vigorous stirring to a slurry containing colloidal silica (15400 parts by weight), tetrapropylammonium bromide (TPABr) (2457 parts by weight), water (16747 parts by weight), and 54 by weight MFI seeds to provide a synthesis mix. The mix was stirred until a homogeneous consistency was obtained. The molar composition of the mix, excluding seeds, was 80 SiO.sub.2 /1 Al.sub.2 O.sub.3 /3.6 Na.sub.2 O/7.2 TPABr/1168 H.sub.2 O. The mix (10 L) was placed in an autoclave and heated while stirring with a single blade turbine (0.8 M/sec tip speed). In 6 hours a temperature of 150.degree. C. was reached at autogenous pressure. The heat up time between 140.degree. C. and 150.degree. C. was 20 min. The stirring was stopped and the mixture was allowed to crystallize without further agitation at 150.degree. C. for 20 hours. After crystallization, a sample was taken. X-ray diffraction analysis showed the product was fully crystalline. Laser light scattering was used to determine the crystal size of the resulting crystals. The mass mean crystal diameter of the crystals and the amount of crystals less than 1 micron diameter is shown below in Table I.
#A synthesis mix was prepared as described in Example 1. The mix (36 L) was placed in an autoclave and heated while stirring with a single blade turbine (0.8 M/sec tip speed). In 5 hours, a temperature of 130.degree. C. was reached at autogenous pressure. The stirring was stopped and heating was continued in a static mode for 7 hours until a temperature of 150.degree. C. was reached. The mixture was allowed to crystallize without further agitation at 150.degree. C. for 20 hours. After crystallization, a sample was taken. X-ray diffraction analysis showed the product was fully crystalline. Laser light scattering was used to determine the crystal size of the resulting crystals. The mass mean crystal diameter of the crystals and the amount of crystals less than 1 micron diameter is shown below in Table I.