Shaped binderless titanosilicate zeolite ts-1

Abstract

There is provided a shaped, binderless catalyst comprising titanosilicate TS-1 and TS-1 precursors; wherein the catalyst is shaped into particles with a defined cross sectional diameter. There is provided a shaped, binderless catalyst, comprising sufficient moisture to retain a desired shape and comprising at least 95 weight percent titanosilicate TS-1 and titanosilicate TS-1 precursors. There is also provided a crystalline titanosilicate zeolite TS-1, having a) shaped, binderless particles with a defined cross sectional diameter, and b) a crystallite size of less than 0.2 micron.

Description

[0001]This application is a divisional patent application, and it claims the benefit of the co-pending prior nonprovisional application Ser. No. 11 / 226,609, filed Sep. 13, 2005. This divisional application is being filed as the result of a restriction requirement. The USPTO classification of this divisional application is 502, subclass 64. The assigned art unit of the parent application is 4116.FIELD OF THE INVENTION[0002]The present invention relates to a process for producing crystalline titanosilicate zeolite TS-1 from a reaction mixture which contains only sufficient water to form zeolite TS-1. As used herein, the terms “titanosilicate zeolite TS-1”, “zeolite TS-1”, or simply TS-1 refers to zeolites having the framework topology of ZSM-5 which contain titanium atoms in their framework structure.BACKGROUND[0003]Prior art methods of preparing crystalline zeolite TS-1 typically produce finely divided crystals which must be separated from an excess of liquid in which the zeolite is ...

AI Technical Summary

Benefits of technology

[0024]One advantage of the present invention is that the reaction mixture may be formed into a desired shape before the crystallization step, thereby reducing the number of process steps required to prepare catalytic materials containing the resulting zeolite. Prior to forming the reaction mixture, it may be necessary to change the liquid content of the reaction mixture, either by drying or by adding more liquid, in order to provide a formable mass which retains its shape. In general, for most shaping methods, water will generally comprise from about 20 percent to about 60 percent by weight, and preferably from about 30 percent to about 50 percent by weight of the reaction mixture.

[0025]The reaction mixture can be formed into a shape, referred to herein as “particles”. Methods for preparing such shapes are well known in the art, and include, for example, extrusion, granulation, agglomerization and the like. When the shape is in the form of particles, they are preferably of a size and shape desired for the ultimate catalyst, and may be in the form of, for example, extrudates, cylinders, spheres, granules, agglomerates and prills. The particles will generally have a cross sectional diameter between about 1 / 32 inch and about ½ inch, and preferably between about 1 / 64 inch and about ¼ inch, i.e., the particles will be of a size to be retained on a 1 / 32 inch, and preferably on a 1 / 64 inch screen and will pass through a ½ inch, and preferably through a ¼ inch screen.

[0026]The shape prepared from the reaction mixture will contain sufficient water to retain a desired shape. Additional water is not required in the mixture in order to initiate or maintain crystallization within the shaped reaction mixture. Indeed, it may be preferable to remove some of the excess water from the shaped reaction mixture prior to crystallization. Conventional methods for drying wet solids can be used to dry the reaction mixture, and may include, for example drying in air or an inert gas such as nitrogen or helium at temperatures below about 200° C. and at pressures from subatmospheric to about 5 atmospheres pressure.

[0027]It should be noted that, while the reaction mixture of the present invention is capable of being formed into and retaining a shape, it need not be shaped prior to formation of the TS-1 crystals. For instance, the reaction mixture may be in the form of a paste-like mass having no particular shape or profile. Also, the resulting TS-1 product need not have any particular shape and may, in fact, simply be in the form of a powder.Zeolite Crystallization

[0028]According to the present process, the zeolite is crystallized either within the reaction mixture or within the shape made from the reaction mixture. In either case, the composition of the mixture from which the zeolite is crystallized has the molar composition ranges stated above.

[0029]It is preferred that the total volatiles content of the reaction mixture during crystallization be in the range of between about 20 wt. % and about 60 wt. %, and preferably between about 30 wt. % and about 60 wt. %, based on the weight of the reaction mixture, where the total volatiles content is the measure of total volatile liquid, including water, in the reaction mixture. It is a feature of the present process that no additional liquid beyond that required to produce the zeolite TS-1 is required for zeolite crystallization.

Problems solved by technology

The liquid, in turn, must be treated for reuse or else be discarded, with potentially deleterious environmental consequences.

These binding and forming steps greatly increase the complexity of catalyst manufacture involving zeolitic materials.

The additional steps may also have an adverse effect on the catalytic performance of the zeolite so bound and formed.

Images