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Solubility, racemates

The hydrochloride addition salt of the above reaction product was prepared in customary fashion, that is, by reaction with hydrochloric acid, followed by fractional crystallization from a mixture of alcohol and ether. The two possible racemic forms were obtained thereby. The difficultly soluble racemate had a melting point of 169° to 170°C and the more readily soluble racemate had a boiling point of 145° to 148°C. [Pg.362]

Scheme 9.28). Despite the modest enantioselectivity, we knew from our previous work that upgrade of enantiomeric purity was possible via preferential removal of the less soluble racemic material by crystallization. In this manner, after a carbon treatment to achieve acceptable levels of residual rhodium, racemic 1 was removed by partial crystallization, followed by subsequent isolation of 1 as a crystalline solid in 72% yield from 22, and in 98.5% ee. [Pg.266]

Synthesis (Pohland, 1953 1955 1963 janssen and Karel (Janssen)1956 Sullivan et al., 1963) In the Grignard reaction of 3-dimethylamino-2-methyl-1-phenyl-propan-lone with benzylmagnesium chloride 4-dimethylamino-3-methyl-1,2-diphenyl-butan-2-ol is formed. The preferred product is the a-diastereomer(75 % a-form, 15 % p-form). The a-form crystallizes and the diastereomeric p-form remains in solution, because of its better solubility. Racemic resolution to obtain the analgetically (+) enantiomer can be achieved on the pure a-Grignard product via fractional crystallization of the salts with D-camphorsulfonic acid. Alternatively the resolution can be achieved by treating the racemic mannich product 3-dimethylamino-2-methyl-1-phenyl-propan-1-one with (-)-dibenzoyltartaric acid in acetone as solvent. [Pg.182]

Temperature (°C) Solubility (+)-mandelic acid (mg/mL) Solubility racemic mandelic acid (mg/mL)... [Pg.186]

Solubility racemate sol ethanol (10 g/100 mL), sol methanol (3 g/100 mL), slightly sol water and other organic solvents. Enantiomer sol ethanol (6 g/100 mL), sol methanol (2 g/ 100 mL), slightly sol water and other organic solvents. [Pg.97]

In general, kinetic resolution requites the presence of a racemic mixture (conglomerate) and the absence of a (generally lower-solubility) racemic compound (both enantiomers in the crystal lattice). This is not always the case, however, and depending on the relative rates of nucleation and crystal growth of the respective forms, a kinetic (nonthermodynamic) isomer separation can sometimes be effected even when a racemic compound is possible. In the case of solid solution of the enantiomers (no lattice fit requirement), an equilibrium process will essentially always be requited. [Pg.260]

The gelatinous Z-bromide tartrate is triturated with warm cone. HBr. The sparingly soluble racemic bromide tartrate which separates out is removed by filtration. On standing, the solution deposits crystals of Z-bromide, which are recrystallized from hot water. [Pg.1539]

Racemic acid, ( )-tartaric acid, is a compound of the two active forms. M.p. 273 C (with IHjO), m.p. 205°C (anhydrous). Less soluble in water than (-t-)-tartaric acid. Formed, together with mesotartaric acid, by boiling (4-)-tartaric acid with 30% NaOH solution, or by oxidation of fumaric acid. Potassium hydrogen racemate is very insoluble. [Pg.385]

Mesotartaric acid crystallizes in plates (IHjO), m.p. 140 C (anhydrous). Very soluble in water. Obtained from the mother-liquors in the preparation of racemic acid or by oxidation of maleic acid. Potassium hydrogen mesotartrale is soluble in water. [Pg.385]

The melting-points of the dextto and laevo forms of any optically active compound may, as in this case, be virtually identical with that of the racemic fomi in many compounds however there is a marked difference in melting-point, and often in solubility, between the (-)-) and ( -) forms on one hand and the ( ) form on the other. [Pg.148]

Acetophenone similarly gives an oxime, CHjCCgHjlCtNOH, of m.p. 59° owing to its lower m.p. and its greater solubility in most liquids, it is not as suitable as the phenylhydrazone for characterising the ketone. Its chief use is for the preparation of 1-phenyl-ethylamine, CHjCCgHslCHNHj, which can be readily obtained by the reduction of the oxime or by the Leuckart reaction (p. 223), and which can then be resolved by d-tartaric acid and /-malic acid into optically active forms. The optically active amine is frequently used in turn for the resolution of racemic acids. [Pg.258]

Both of the alkaloids anhalamine (62) from l ophophora williamsii and lophocerine (63) from l ophocereus schotti were isolated (after the properties of purified mescaline had been noted) in the search for materials of similar behavior. Interestingly, lophocerine, isolated as its methyl ether, after dia2omethane treatment of the alkaU-soluble fraction of total plant extract, is racemic. It is not known if the alkaloid in the plant is also racemic or if the isolation procedure causes racemization. [Pg.541]

The last mother liquors contain mesotaitanc acid, in. p. 1.4. 3 144°, which is much more soluble in water than racemic ju ici. To obtain a pme specimen repeated crystallisation is necesstiry. [Pg.122]

Another possibility of constructing a chiral membrane system is to prepare a solution of the chiral selector which is retained between two porous membranes, acting as an enantioselective liquid carrier for the transport of one of the enantiomers from the feed solution of the racemate to the receiving side (Fig. 1-5). This system is often referred to as membrane-assisted separation. The selector should not be soluble in the solvent used for the elution of the enantiomers, whose transport is driven by a gradient in concentration or pH between the feed and receiving phases. As a drawback common to all these systems, it should be mentioned that the transport of one enantiomer usually decreases when the enantiomer ratio in the permeate diminishes. Nevertheless, this can be overcome by designing a system where two opposite selectors are used to transport the two enantiomers of a racemic solution simultaneously, as it was already applied in W-tube experiments [171]. [Pg.15]

Another important issue that must be considered in the development of CSPs for preparative separations is the solubility of enantiomers in the mobile phase. For example, the mixtures of hexane and polar solvents such as tetrahydrofuran, ethyl acetate, and 2-propanol typically used for normal-phase HPLC may not dissolve enough compound to overload the column. Since the selectivity of chiral recognition is strongly mobile phase-dependent, the development and optimization of the selector must be carried out in such a solvent that is well suited for the analytes. In contrast to analytical separations, separations on process scale do not require selectivity for a broad variety of racemates, since the unit often separates only a unique mixture of enantiomers. Therefore, a very high key-and-lock type selectivity, well known in the recognition of biosystems, would be most advantageous for the separation of a specific pair of enantiomers in large-scale production. [Pg.61]

To evaluate the economics of this process, a cost model has been developed to estimate the separation costs for a specific racemate [68, 69]. For this purpose, the sensitivity of the separation costs for several key process parameters have been established as compared to a base-case separation in which a purity of 99 % is required at an enantioselectivity of 1.15. The maximum solubility of the drug is set... [Pg.143]

Chemical development Proof of structure and configuration are required as part of the information on chemical development. The methods used at batch release should be validated to guarantee the identity and purity of the substance. It should be established whether a drug produced as a racemate is a true racemate or a conglomerate by investigating physical parameters such as melting point, solubility and crystal properties. The physicochemical properties of the drug substance should be characterized, e.g. crystallinity, polymorphism and rate of dissolution. [Pg.325]

Meso compounds contain chirality centers but are achiral overall because they have a plane of symmetry. Racemic mixtures, or racemates, are 50 50 mixtures of (+) and (-) enantiomers. Racemic mixtures and individual diastereomers differ in their physical properties, such as solubility, melting point, and boiling point. [Pg.322]

In a catalytic asymmetric reaction, a small amount of an enantio-merically pure catalyst, either an enzyme or a synthetic, soluble transition metal complex, is used to produce large quantities of an optically active compound from a precursor that may be chiral or achiral. In recent years, synthetic chemists have developed numerous catalytic asymmetric reaction processes that transform prochiral substrates into chiral products with impressive margins of enantio-selectivity, feats that were once the exclusive domain of enzymes.56 These developments have had an enormous impact on academic and industrial organic synthesis. In the pharmaceutical industry, where there is a great emphasis on the production of enantiomeri-cally pure compounds, effective catalytic asymmetric reactions are particularly valuable because one molecule of an enantiomerically pure catalyst can, in principle, direct the stereoselective formation of millions of chiral product molecules. Such reactions are thus highly productive and economical, and, when applicable, they make the wasteful practice of racemate resolution obsolete. [Pg.344]

Despite its widespread application [31,32], the kinetic resolution has two major drawbacks (i) the maximum theoretical yield is 50% owing to the consumption of only one enantiomer, (ii) the separation of the product and the remaining starting material may be laborious. The separation is usually carried out by chromatography, which is inefficient on a large scale, and several alternative methods have been developed (Figure 6.2). For example, when a cyclic anhydride is the acyl donor in an esterification reaction, the water-soluble monoester monoacid is separable by extraction with an aqueous alkaline solution [33,34]. Also, fiuorous phase separation techniques have been combined with enzymatic kinetic resolutions [35]. To overcome the 50% yield limitation, one of the enantiomers may, in some cases, be racemized and resubmitted to the resolution procedure. [Pg.135]

Our approach for chiral resolution is quite systematic. Instead of randomly screening different chiral acids with racemic 7, optically pure N-pMB 19 was prepared from 2, provided to us from Medicinal Chemistry. With 19, several salts with both enantiomers of chiral acids were prepared for evaluation of their crystallinity and solubility in various solvent systems. This is a more systematic way to discover an efficient classical resolution. First, a (+)-camphorsulfonic acid salt of 19 crystallized from EtOAc. One month later, a diastereomeric (-)-camphorsulfonic acid salt of 19 also crystallized. After several investigations on the two diastereomeric crystalline salts, it was determined that racemic 7 could be resolved nicely with (+)-camphorsulfonic acid from n-BuOAc kinetically. In practice, by heating racemic 7 with 1.3equiv (+)-camphorsulfonic acid in n-BuOAc under reflux for 30 min then slowly cooling to room temperature, a cmde diastereomeric mixture of the salt (59% ee) was obtained as a first crop. The first crop was recrystallized from n-BuOAc providing 95% ee salt 20 in 43% isolated yield. (The optical purity was further improved to -100% ee by additional recrystallization from n-BuOAc and the overall crystallization yield was 41%). This chiral resolution method was more efficient and economical than the original bis-camphanyl amide method. [Pg.7]


See other pages where Solubility, racemates is mentioned: [Pg.271]    [Pg.178]    [Pg.95]    [Pg.271]    [Pg.178]    [Pg.95]    [Pg.46]    [Pg.385]    [Pg.143]    [Pg.239]    [Pg.215]    [Pg.526]    [Pg.273]    [Pg.32]    [Pg.388]    [Pg.267]    [Pg.142]    [Pg.5]    [Pg.341]    [Pg.63]    [Pg.791]    [Pg.92]    [Pg.126]    [Pg.151]    [Pg.98]    [Pg.24]    [Pg.161]    [Pg.162]    [Pg.20]   
See also in sourсe #XX -- [ Pg.370 , Pg.375 ]




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