Claims
- 1. A process for the production of a polyribosylribitol phosphate (PRP) oligomer, which comprises:
- coupling a compound of the formula: ##STR12## wherein R.sub.1 is a first protecting group and R.sub.2 is a second protecting group, to a solid polyethylene glycol monoethyl ether (PEG) support to form a PEG-supported compound,
- dissolving said PEG-supported compound in a solvent,
- removing said first protecting group from said PEG-supported compound to form a deprotected PEG-supported compound,
- coupling the deprotected PEG-supported compound with a repeating unit for chain elongation of the formula: ##STR13## removing the protecting group from the phosphorus atom to form a PEG-supported synthetic PRP,
- removing said PEG-supported synthetic PRP in solid form from said solvent to separate the PEG-supported synthetic PRP from by-products,
- redissolving said PEG-supported synthetic PRP in solid form in a solvent,
- repeating said step of removing said first protecting group, coupling with the repeating unit, removing the protecting group from the phosphorus atom, removing PEG-supported synthetic PRP in solid form from the solvent and redissolving PEG-supported synthetic PRP in solid form in a solvent until a desired number of repeating units in the PRP oligomer has been assembled,
- terminating the oligomer with a chain-terminating molecule of the formula: ##STR14## wherein m is an integer from 4 to 6 and R.sub.3 is a third protecting group to produce a PEG-bound protected PRP oligomer,
- removing the protecting group from the phosphorus atom, and
- removing said PEG-bound protected PRP oligomer in solid form from said solvent to separate the PEG-bound protected PRP oligomer of the formula: ##STR15## wherein n is an integer from 3 to 20 and X.sup.+ is a counter ion.
- 2. The process of claim 1 wherein said purified PEG-bound protected oligomer is cleaved from said PEG support to provide a compound of the formula: ##STR16## and removing said second and third protecting groups to provide an unbound unprotected PRP oligomer.
- 3. The process of claim 2 wherein R.sub.2 is benzyl, R.sub.1 is dimethoxytrityl and R.sub.3 is monomethoxytrityl.
- 4. The process of claim 2 wherein said counter ion is ammonium.
- 5. The process of claim 2 including converting the unbound unprotected PRP oligomer to a synthetic PRP oligomer represented by the formula: ##STR17## wherein R is a linker fragment.
- 6. The process of claim 5 wherein said linker fragment has the formula --CH.sub.2 (CH.sub.2).sub.m --X in which m is an integer and X is a chemically-reactive functional group, an amino reactive group or a photoactivatable group.
- 7. The process of claim 6 wherein the counter ion is a sodium ion.
- 8. The process of any one of claims 1 to 7 wherein said polyethylene glycol has a loading capacity of about 200 to 500 .mu.mol/g of support.
Priority Claims (1)
Number |
Date |
Country |
Kind |
9202219 |
Mar 1992 |
GBX |
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Parent Case Info
This is a continuation of application Ser. No. 08/256,839 filed Oct. 3, 1994, which is a 371 application of PCT/CA93/00041, filed Mar. 2, 1993.
US Referenced Citations (1)
Number |
Name |
Date |
Kind |
5034519 |
Beuverly et al. |
Jul 1991 |
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Foreign Referenced Citations (1)
Number |
Date |
Country |
0276516 |
Aug 1988 |
EPX |
Continuations (1)
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Parent |
256839 |
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