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Molecular Sieve Patent

 

Method for the preparation of crystalline molecular sieve materials wherein the organic template is an enantiomer

Molecular sieve abstract

Crystalline molecular sieve materials such as high silica zeolites are manufactured using an organic template comprising an optically active enantiomer such as an enantiomer of 3(.+-.) methyl piperidine -N,N-dimethyl bromide. A new zeolite materials is identified.

Molecular sieve claims

We claim:

1. A process for the production of a synthetic crystalline molecular sieve material by the use of a reaction mixture containing an organic template material characterised in that the template is an enantiomer.

2. A process as claimed in claim 1 wherein the template is an amine or ammonium enantiomer.

3. A process as claimed in claim 2 wherein the template is an piperidine enantiomer.

4. A process as claimed in claim 1 for the production of a crystalline high silica zeolite molecular sieve comprising forming an aqueous reaction mixture containing a template comprising an enantiomer and sources of R.sub.2 O.sub.3 SiO.sub.2 and optionally M.sub.2 O.sub.3 in the molar proportions ##EQU2## wherein R indicates an alkali metal and M indicates one or more metals selected from B, Al, V, Cr, Mr, Fe, Ga, As, Mo or Sb, hydrothermally treating the reaction mixture at a temperature of from 100.degree. C. to 300.degree. C. and a pressure of from 1 to 100 bars until crystallisation occurs and separating the crystalline product so formed.

5. A process as claimed in claim 4 wherein the molar proportions of the reactants are ##EQU3## and R is Na and M is Al.

Molecular sieve description

BACKGROUND OF THE INVENTION

1. Field of the Invention

This invention relates to a novel process for the preparation of crystalline, synthetic molecular sieve materials and materials so produced.

2. Summary of the Invention

By `molecular sieve` is meant herein microporous three dimensional framework materials having pores generally in the 2 to 20 Angstroms size range which are capable of use for molecular separations. The framework may consist of or comprise, for example, aluminosilicate, aluminophosphate or silica.

According to one aspect of the present invention there is provided a process for the production of a synthetic crystalline molecular sieve material characterised by the use in the reaction mixture of an organic template comprising an optically active enantiomer. It has now been found that by the use of the novel templates described above the synthesis may be controlled to produce different products than would be produced using the corresponding racemic form of the template and that novel zeolites may be produced thereby.

The present invention is particularly, although not exclusively, concerned with the preparation of high silica zeolites or their silica analogues. By "high silica zeolite" is meant a zeolite having the general formula:

where R is one or more alkali metal or alkaline earth metals of valency n preferably sodium, M.sub.2 O.sub.3 is an oxide of one or more of B, Al, V, Cr, Mn, Fe, Ga, As, Mo or Sb but preferably Al, x is a charge balancing quantity of R, y is from 0 to 1 z is more than 6 for example from 10 to 5000 and W is at least 0 for example from 0 to 2000. While zeolites having a lesser content of silica such as the traditional zeolites A, X and Y may be manufactured readily without the assistance of an organic template material high silica zeolites are generally synthesised with the assistance of an organic template material present in the reaction medium. Such synthesis may be accomplished by including sources of the constituents of the zeolite in an aqueous reaction medium containing the template material and heating, generally, under elevated pressure until crystallisation has taken place. Very suitably the proportions of the sources of the constituents are such as to provide a reaction medium having the following composition in terms of oxide mole ratios. ##EQU1## where R, and M have the values above defined. Suitably, the alkali metal may be provided by the hydroxide and/or by the use of an alkali metal silicate; the SiO.sub.2 may be provided by the use of a silica hydrosol or gel, by silicic acid or by said sodium silicate; and the metal M may be provided by the sodium metallate, for example, aluminate or by the use of a metallosilicate, for example aluminosilicate. Alternative sources of the desired ingredients will be well known to those versed in the art. Suitably, the synthesis may be carried out under alkaline conditions, at a temperature of from 100.degree. C. to 300.degree. C. and at a pressure of from about 1 to 100 bars which may, if desired, be generated autogenously. The zeolite so formed may be separated, washed free of residual reaction medium, dried and calcined to remove residual template materials and/or to reduce or remove water of crystallisation.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. I is an x-ray diffraction pattern obtained upon the product of the preparation I(a) obtained in the Example I.

FIG. II is the NMR spectra (29.sub.si MAS) obtained on the product of Preparation I(a) of Example I.

FIG. III is the isotherm for adsorption of isobutane on the product of Preparation I(a), Example I.

FIG. IV is an X-ray diffraction pattern of a novel zeolite of the invention.

FIG. V is an X-ray diffraction pattern of the product of synthesis (b) in Example I.

DETAILED DESCRIPTION OF THE INVENTION

Very many specific zeolite synthesis have been described in detail in the literature and many of these are summarised in the book "Molecular Sieves" by D. W. Breck (1974 John Wiley & Sons). A major characteristic of these syntheses is not the mole ratio of reactants, although this may to an extent be tailored to the type of zeolite required, but the particular organic template to be used to produce a desired zeolite type. British Pat. No. 1161974 for example, specifies the use of a tetrapropyl ammonium hydroxide template to produce zeolite ZSM5 the oxide mole ratios of reactions being specified very broadly as follows:

The templates specifically disclosed above are substantially all non-optically active and incapable of existing as racemates. An exception to this is 3-methyl piperidine which is listed as being suitable for use in the synthesis of an aluminophosphate molecular sieve (ALPO-5). This compound exists as a racemate.

An enantiomer of 3-methyl piperidine may be prepared by separation from the racemate, for example by the process described in our copending European Patent Application claiming the same priority dates as the present application or by direct synthesis. The process of said European Patent Application is to utilise a crystalline molecular sieve having an assymetric crystal structure such as zeolite ZSM11 zeolite Theta I or silicalite II, the silica analogue of ZSM11 which are assymetric zeolites and may be prepared as described in British Pat. No. 1339501 European Patent Specification No. 0057049 and Nature Vol 280 Aug. 23 1979 pages 664-665 respectively as a stereoselective adsorbent for one enantiomer of a racemate, the channels of the molecular sieve being partially blocked, when that molecular sieve is not itself enantiomorphic, by an enantiomer separable from those which constitute the racemate being adsorbed. By such means an eluate relatively concentrated in one enantiomer may be produced and the concentration thereof may be increased as required by recycling.

Examples of other enantiomers which may be used according to the present invention are compounds belonging to the groups quaternary ammonium compounds, amines, alcohols, and heterocyclic compounds and may be selected, for example, from the list of chiral building blocks on pages 1067 to 1069 of the FLUKA (Fluorochem Limited) Catalogue No. 14 1984-5 for example alphapinene, 2 methyl butanol or piperidium compounds such as the 3-methyl piperidine-N,N-dimethyl cation or a cobalt interpenetration complex as Co.sup.+3 bis(ethylene diamine) or other Co.sup.+3 complexes with low molecular weight ligands containing for example not more than 4 carbon atoms.

There is a growing need for more, or relatively concentrated, enantiomers which, although they may be common in nature are often produced in the racemic form by synthesis. One method for achieving the required separation is by stereoselective adsorption of one enantiomer onto an assymetric crystalline molecular sieve as disclosed above.

It is postulated that the zeolites produced by the present invention may be assymetric either in the sense of possessing two sets of pores of opposite symmetry, or in the sense of being enantiomeric and that, if so, they may exhibit chiral adsorption properties relative to racemic mixtures.


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