Claims
- 1. In the process for the production of a conventional penicillin having the formula ##STR55## wherein ##STR56## is the residue after removal of the hydroxyl group of an organic carboxylic acid containing from two to twenty carbon atoms
- which comprises the consecutive steps of acylating with the acid chloride of said organic carboxylic acid a silylated nucleus having the formula ##STR57## wherein B is an easily cleavable ester protecting group and then converting group B to hydrogen,
- the improvement which comprises, prior to acylation, converting said silylated nucleus to a compound of the formula ##STR58## wherein B has the same meaning as above, by adding dry carbon dioxide to a solution of said silylated nucleus in an anhydrous inert organic solvent at a temperature in the range of 0.degree. C. to 100.degree. C. until completion of the carbonylation reaction.
- 2. In the process for the production of a conventional penicillin having the formula ##STR59## wherein ##STR60## is the residue after removal of the hydroxyl group of an organic carboxylic acid containing from two to twenty carbon atoms
- which comprises the consecutive steps of acylating with the acid chloride of said organic carboxylic acid a silylated nucleus having the formula ##STR61## wherein B is an easily cleavable ester protecting group selected from the group consisting of trimethylsilyl, benzyhydryl, benzyl, p-nitrobenzyl, p-methoxybenzyl, trichloroethyl, phenacyl, acetonyl, methoxymethyl, 5-indanyl, 3-phthalidyl, 1-[(ethoxycarbonyl)oxy]ethyl, pivaloyloxymethyl and acetoxymethyl and then converting group B to hydrogen,
- the improvement which comprises, prior to acylation, converting said silylated nucleus to a compound of the formula ##STR62## wherein B has the same meaning as above, by adding dry carbon dioxide to a solution of said silylated nucleus in an anhydrous inert organic solvent at a temperature in the range of 0.degree. C. to 100.degree. C. until completion of the carbonylation reaction.
- 3. In the process for the production of a conventional penicillin having the formula ##STR63## wherein ##STR64## is the residue after removal of the hydroxyl group of an organic carboxylic acid containing from two to twenty carbon atoms
- which comprises the consecutive steps of acylating with the acid chloride of said organic carboxylic acid the silylated nucleus having the formula ##STR65## and then converting the trimethylsilyl group on the acylated product to hydrogen,
- the improvement which comprises, prior to acylation, converting said silylated nucleus to a compound of the formula ##STR66## by adding dry carbon dioxide to a solution of said silylated nucleus in an anhydrous inert organic solvent at a temperature in the range of 0.degree. C. to 100.degree. C. until completion of the carbonylation reaction.
- 4. In the process of claim 2 for the production of a conventional penicillin having the formula ##STR67## wherein ##STR68## is the residue after removal of the hydroxyl group of an organic carboxylic acid containing from two to twenty carbon atoms and B is 5-indanyl
- which comprises acylating with the acid chloride of said organic carboxylic acid the silylated nucleus having the formula ##STR69## wherein B is as above the improvement which comprises, prior to acylation, converting said silylated nucleus to a compound of the formula ##STR70## wherein B has the same meaning as above, by adding dry carbon dioxide to a solution of said silylated nucleus in an anhydrous inert organic solvent at a temperature in the range of 0.degree. C. to 100.degree. C. until completion of the carbonylation reaction.
- 5. In the process of claim 2 for the production of a conventional penicillin having the formula ##STR71## wherein ##STR72## is the residue after removal of the hydroxyl group of an organic carboxylic acid containing from two to twenty carbon atoms and B is 3-phthalidyl
- which comprises acylating with the acid chloride of said organic carboxylic acid the silylated nucleus having the formula ##STR73## wherein B is as above the improvement which comprises, prior to acylation, converting said silylated nucleus to a compound of the formula ##STR74## wherein B has the same meaning as above, by adding dry carbon dioxide to a solution of said silylated nucleus in an anhydrous inert organic solvent at a temperature in the range of 0.degree. C. to 100.degree. C. until completion of the carbonylation reaction.
- 6. In the process of claim 2 for the production of a conventional penicillin having the formula ##STR75## wherein ##STR76## is the residue after removal of the hydroxyl group of an organic carboxylic acid containing from two to twenty carbon atoms and B is 1[(ethoxycarbonyl)oxy]ethyl
- which comprises acylating with the acid chloride of said organic carboxylic acid the silylated nucleus having the formula ##STR77## wherein B is as above the improvement which comprises, prior to acylation, converting said silylated nucleus to a compound of the formula ##STR78## wherein B has the same meaning as above, by adding dry carbon dioxide to a solution of said silylated nucleus in an anhydrous inert organic solvent at a temperature in the range of 0.degree. C. to 100.degree. C. until completion of the carbonylation reaction.
- 7. In the process of claim 2 for the production of a conventional penicillin having the formula ##STR79## wherein ##STR80## is the residue after removal of the hydroxyl group of an organic carboxylic acid containing from two to twenty carbon atoms and B is pivaloyloxymethyl
- which comprises acylating with the acid chloride of said organic carboxylic acid the silylated nucleus having the formula ##STR81## wherein B is as above the improvement which comprises, prior to acylation, converting said silylated nucleus to a compound of the formula ##STR82## wherein B has the same meaning as above, by adding dry carbon dioxide to a solution of said silylated nucleus in an anhydrous inert organic solvent at a temperature in the range of 0.degree. C. to 100.degree. C. until completion of the carbonylation reaction.
- 8. In the process of claim 2 for the production of a conventional penicillin having the formula ##STR83## wherein ##STR84## is the residue after removal of the hydroxyl group of an organic carboxylic acid containing from two to twenty carbon atoms and B is acetoxymethyl
- which comprises acylating with the acid chloride of said organic carboxylic acid the silylated nucleus having the formula ##STR85## wherein B is as above the improvement which comprises, prior to acylation, converting said silylated nucleus to a compound of the formula ##STR86## wherein B has the same meaning as above, by adding dry carbon dioxide to a solution of said silylated nucleus in an anhydrous inert organic solvent at a temperature in the range of 0.degree. C. to 100.degree. C. until completion of the carbonylation reaction.
- 9. The process for the production of a 6-.alpha.-aminoarylacetamidopenicillanic acid which comprises reacting a compound of the formula ##STR87## in an anhydrous inert organic solvent at a temperature above -10.degree. C. but not above 25.degree. C. with approximately an equimolar weight of a D-(-)-.alpha.-aminoarylacetyl chloride hydrochloride added in at least four portions over a period of at least two hours followed by hydrolysis with cold water and then isolation of the 6-.alpha.-aminoarylacetamidopenicillanic acid by conventional methods.
- 10. The process for the production of amoxicillin which comprises reacting a compound of the formula ##STR88## in an anhydrous inert organic solvent at a temperature above -10.degree. C. but not above 25.degree. C. with approximately an equimolar weight of D-(-)-2-p-hydroxyphenylglycyl chloride hydrochloride added in at least four portions over a period of at least two hours followed by hydrolysis with cold water and then isolation of the amoxicillin by conventional methods.
- 11. The process for the production of ampicillin which comprises reacting a compound of the formula ##STR89## in an anhydrous inert organic solvent at a temperature above -10.degree. C. but not above 25.degree. C. with approximately an equimolar weight of D-(-)-2-phenylglycyl chloride hydrochloride added in at least four portions over a period of at least two hours followed by hydrolysis with cold water and then isolation of the ampicillin by conventional methods.
CROSS-REFERENCE TO RELATED APPLICATIONS
This application is a continuation-in-part of our prior, copending application Ser. No. 21,852 filed Mar. 19, 1979, now U.S. Pat. No. 4,240,960, which in turn was a continuation-in-part of our prior, copending application Ser. No. 4,780 filed Jan. 19, 1979 and now abandoned which in turn was a continuation-in-part of our prior, copending application Ser. No. 970,704 filed Dec. 18, 1978, and now abandoned.
US Referenced Citations (17)
Foreign Referenced Citations (5)
Number |
Date |
Country |
938321 |
Oct 1963 |
GBX |
959853 |
Jun 1964 |
GBX |
962719 |
Jul 1964 |
GBX |
1008468 |
Oct 1965 |
GBX |
1339605 |
Dec 1973 |
GBX |
Continuation in Parts (3)
|
Number |
Date |
Country |
Parent |
21852 |
Mar 1979 |
|
Parent |
4780 |
Jan 1979 |
|
Parent |
970704 |
Dec 1978 |
|