Claims
- 1. A substantially pure neocarzinostatin derivative having the formula (A):
- (SMA)-(NCS)-(SMA) (A)
- wherein (NCS) is a divalent neocarzinostatin residue and (SMA) comprises the monovalent residue of a styrene-maleic acid copolymer having a weight-average molecular weight of from 800 to 2,500, said (NCS) residue being bonded to said (SMA) residues via amide linkages formed between primary amino groups of the neocarzinostatin molecule and carbonyl groups of the styrene-maleic acid copolymer.
- 2. The neocarzinostatin derivative as defined by claim 1, said styrene-maleic acid copolymer comprising (a) styrene residues, (b) maleic acid residues and (c) residues of the formula: ##STR9##
- 3. The neocarzinostatin derivative as defined by claim 2, wherein the molar ratio of the residues (a) to the sum of the residues (b) and (c) ranges from about 1:1 to 1.3:1.
- 4. The neocarzinostatin derivative as defined by claim 3, wherein the molar ratio of the residues (a) to the sum of the residues (b) and (c) is about 1:1.
- 5. The neocarzinostatin derivative as defined by claim 2, said primary amino groups of the neocarzinostatin molecule comprising the alanine residue at the N-terminal and the lysine residue at the 20th position thereof.
- 6. The neocarzinostatin derivative as defined by claim 1, said styrene-maleic acid copolymer comprising a partially hydrolyzed styrene-maleic anhydride copolymer.
- 7. The neocarzinostatin derivative as defined by claim 3, wherein the molar ratio of the residues (b) to the residues (c) ranges from 85:15 to 35:65.
- 8. The neocarzinostatin derivative as defined by claim 7, wherein the molar ratio of the residues (b) to the residues (c) ranges from 80:20 to 40:60.
- 9. A process for the preparation of a neocarzinostatin derivative, comprising reacting neocarzinostatin, in an aqueous reaction medium, with a molar excess of a partially hydrolyzed styrene-maleic anhydride copolymer, said copolymer satisfying the formulae (B) and (C):
- 800.ltoreq.Mw.ltoreq.2,500 (B)
- Mw/Mn.ltoreq.1.5-1.1-10.sup.-4 Mw (C)
- wherein Mw is the weight-average and Mn the number-average molecular weight thereof.
- 10. The process as defined by claim 9, further comprising isolating the neocarzinostatin derivative of claim 10 from the reaction product thereof.
- 11. The process as defined by claim 10, said isolating being by gel filtration.
- 12. The process as defined by claim 10, comprising reacting 1.5 to 15 parts by weight of said copolymer with 1 part by weight of the neocarzinostatin.
- 13. The process as defined by claim 12, wherein the concentration of the total amount of the neocarzinostatin and the copolymer in said reaction medium ranges from 10 to 35% by weight.
- 14. The process as defined by claim 13, wherein the pH of the reaction medium ranges from 7.5 to 9.5.
- 15. The process as defined by claim 14, wherein the reaction is carried out at a temperature of less than 15.degree. C. under dark conditions.
- 16. The process as defined by claim 11, wherein prior to said gel filtration, the reaction product is preliminarily purified.
- 17. The process as defined by claim 11, wherein said gel filtration is carried out utilizing a substrate having an exclusion limit of 50,000 to 150,000, with globular proteins as the molecular weight standard.
- 18. The process as defined by claim 9, wherein said reactant copolymer is in powder form.
- 19. A composition of matter comprising the neocarzinostatin derivative as defined by claim 1, and a pharmaceutically acceptable carrier therefor.
Priority Claims (1)
Number |
Date |
Country |
Kind |
58-145419 |
Aug 1983 |
JPX |
|
Parent Case Info
This application is a continuation of application Ser. No. 749,679, filed June 28, 1985, now abandoned, which is a continuation of now abandoned U.S. Ser. No. 636,485 of Aug. 1, 1984.
US Referenced Citations (4)
Continuations (2)
|
Number |
Date |
Country |
Parent |
749679 |
Jun 1985 |
|
Parent |
636485 |
Aug 1984 |
|