Organic-inorganic hybrid chiral sorbent and process for the preparation thereof

Abstract

The present invention provides an organic-inorganic hybrid chiral sorbent for chiral resolution of various racemic compounds viz. racemic mandelic acid, 2-phenyl propionic acid, diethyl tartrate, 2,2′-dihydroxy-1,1′-binaphthalene (BINOL) and cyano chromene oxide with excellent chiral separation (enantiomeric excess, 99%) in case of mandelic acid under medium pressure column chromatography. These optically pure enantiomers find applications as intermediates in pharmaceutical industries.

Description

FIELD OF THE INVENTION[0001]The present invention relates to an organic-inorganic hybrid chiral sorbent. More particularly it relates to optically pure covalently bonded amino alcohol to mesoporous silica as chiral selector for chiral resolution of various racemic compounds, viz. racemic mandelic acid, 2-phenyl propionic acid, diethyl tartrate, 2,2′-dihydroxy-1,1′-binaphthalene (BINOL) and cyano chromene oxide under medium pressure column chromatography. The present invention further relates to a process for the preparation of organic-inorganic hybrid chiral sorbent. These optically pure enantiomers find applications as intermediates in pharmaceutical industries.BACKGROUND OF THE INVENTION[0002]Resolution of chiral molecules is required in many areas of research. As enzymes and other biological receptor molecules are stereo-specific, enantiomers of a racemic compound may interact with them in a different manner. Consequently, two enantiomers of a racemic compound have different phar...

AI Technical Summary

Benefits of technology

[0028]Yet another object of the present invention is to provide chiral resolution of racemic compounds using optically pure amino alcohol covalently attached on mesoporous silica as chiral selector for achieving high Enantiomeric Excess (ee) (99%) at room temperature.

Problems solved by technology

The drawbacks of this process are; (i) β-cyclodextrin alone does not recognize enantiomers of mandelic acid; (ii) stationary phase needs to be permethylated for achieving high chiral separation; (iii) reaction has to be conducted in reverse phase.

The drawbacks of this process are; (i) In this study, the amino acid was derivatized using o-phthalaldehyde or naphthalene-2,3-dicarboxaldehyde to allow conventional fluorimetric detection.

Such a derivatization step, however, is undesirable because it prolongs the sample preparation time, and requires additional validation because it may be a potential source of contamination, may induce racemization or may complicate the separation.

The drawbacks of this process are; (i) the need to have dilute perchloric acid as mobile phase for such a column; (ii) The separation of the enantiomers is temperature sensitive.

The drawbacks of this process are; (i) Teicoplanin is a toxic and naturally occurring complex molecule therefore cannot be easily tuned for various applications (ii) due to the presence of many glycosidic linkages it is prone to hydrolysis and / or alteration in conformation thereby change in optical properties under the elution conditions (iii) this separation process requires pH adjustment about 4 and 7; (iv) separation has to be conducted in reverse phase.

The drawbacks of this process are; (i) This work includes only comparison of an ordered mesoporous aluminosilicate, silica, alumina, titania and zirconia in normal-phase high-performance liquid chromatography; (ii) it requires very large column (250×4 mm).

The drawbacks of this process are; (i) only trifluoromethyl group containing compounds are separated.

The drawbacks of this process are; (i) Derivatization of carboxylic acids or eluent modifiers such as acetic acid or diethyl amine is required in this system;.

(ii) Polysaccharide phases based chiral stationary phase is not predictable and capable of separating both t-acid and n-basic type compounds.

The drawbacks of this process is (i) This separation technique requires 200×4.6 mm i.d. stainless-steel column; (ii) only underivatized amino acids were resolved on it; (iii) the use of methanol doesn't favor the resolution of DL-selenomethionine; (iv) higher temperature gives some de-activation effect of some biological sample.

14 (1999) 1333 described chiral resolution and speciation of DL-selenomethionine enantiomers by capillary gas chromatography (GC) using an L-valine-tert-butylamide modified polydimethylsiloxane as chiral stationary phase The drawbacks of this process are; (i) good resolution was achieved in the higher temperature range only from 100-160° C.; (ii) requires He as carrier gas; (iii) separation is more difficult for complex biological samples.

The drawbacks of this process are; (i) This separation technique has been used to separate the enantiomers of selenoamino acids by the addition of chiral additives to the electrophoretic buffer; (ii) UV absorbance detection was used in these studies and required the derivatization of the selenoamino acids to permit detection; (iii) UV absorbance detection, without sample pre-concentration, was not sensitive enough to permit the detection of the low levels of selenoamino acids present in complex samples; (iv) applied voltage and pH value gives variation in separation results; (v) buffer system was chosen for good resolution; (vi) addition of methanol to the buffer is required for improved resolution.

The drawbacks of this process are; (i) enzymetic separation requires different buffer solutions; (ii) the conversion and enantiomeric excess is affected by varying the solvents, enzymes and its concentration; (iii) low enantiomeric excess was achieved through achiral column chromatography by loading 51% compound.

The drawbacks of this process are; (i) enzymes shows very low enantio-selectivity; (ii) it's a time consuming process (more than 7 days); (iii) solvent, such as acetonitrile, cyclohexane, toluene, methyl-t-butyl ether, 2-methyl-2-pentanol, ethyl caprate is required for this system.

The drawbacks of this process are; (i) microorganism is essential to generate the (R)-mandelic acid derivative or (S)-mandelic acid derivative; (ii) requires appropriate buffer solution.

The drawbacks of this process are; (i) The isolation and collection of microbial cells from culture broth is complicated; (ii) buffer solution is required for maintaining pH; (iii) it is time consuming process.

The drawbacks of this process are; (i) hydrolysis of mandelonitrile is necessary; (ii) requires neutral or basic reaction system to produce the (R)-(−)-mandelic acid; (iii) requires expensive use of microorganism and Ghisalba Oreste et at in U.S. Pat. No. 360,802 Jun. 2, 1989 described process for the preparation of R- or S-2-hydroxy-4-phenylbutyric acid in very high enantiomeric purity by enzymatic separation.

Disadvantage of this process are; (i) The reduction of the substrate is effected by the so-called final reductase; (ii) suitable as biocatalysts are only purified enzymes; (iii) regeneration of enzyme is complicated.

The drawbacks of this process are; (i) deactivation of microorganism within a short period of time at higher and lower temperature; (ii) high concentration and high yield is difficult to obtain for alpha-hydroxy acid or alpha-hydroxyamide; (iii) the reaction rate is lowered with an increase in the concentration of the alpha-hydroxy acid or alpha-hydroxyamide product as a result, the reaction does not proceed to completion.

The drawbacks of this process are; (i) chiral reagents and microorganism are more expensive; (ii) this method is industrially non-advantageous for producing (R)-(−)-mandelic acid or derivatives; (iii) hydrogenases produced by these bacteria are not always satisfactory.

The drawbacks of this process are; (i) it requires buffer solution to adjust the pH; (ii) peak-splitting phenomenon was caused by some components of the cation-exchange column or mobile phase.

The drawbacks of this process are; (i) variations in results are found with changing the solvents.