STUDIES ON THE RING-OPENING POLYMERIZATION OF TETRAHYDROFURAN Ⅳ. COPOLYMERIZATION OF TETRAHYDROFURAN AND PROPYLENE OXIDE INITIATED BY FUMING SULFURIC ACID AND PERCHLORIC ACID CATALYST SYSTEM
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STUDIES ON THE RING-OPENING POLYMERIZATION OF TETRAHYDROFURAN Ⅳ. COPOLYMERIZATION OF TETRAHYDROFURAN AND PROPYLENE OXIDE INITIATED BY FUMING SULFURIC ACID AND PERCHLORIC ACID CATALYST SYSTEM
Vol. 1, Issue 1, Pages: 25-31(1983)
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Published:20 July 1983
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ZHANG Hongzhi, GAO Guozhen, WANG Yin, et al. STUDIES ON THE RING-OPENING POLYMERIZATION OF TETRAHYDROFURAN Ⅳ. COPOLYMERIZATION OF TETRAHYDROFURAN AND PROPYLENE OXIDE INITIATED BY FUMING SULFURIC ACID AND PERCHLORIC ACID CATALYST SYSTEM[J]. 1983, 1(1): 25-31.
DOI:
ZHANG Hongzhi, GAO Guozhen, WANG Yin, et al. STUDIES ON THE RING-OPENING POLYMERIZATION OF TETRAHYDROFURAN Ⅳ. COPOLYMERIZATION OF TETRAHYDROFURAN AND PROPYLENE OXIDE INITIATED BY FUMING SULFURIC ACID AND PERCHLORIC ACID CATALYST SYSTEM[J]. 1983, 1(1): 25-31.DOI:
STUDIES ON THE RING-OPENING POLYMERIZATION OF TETRAHYDROFURAN Ⅳ. COPOLYMERIZATION OF TETRAHYDROFURAN AND PROPYLENE OXIDE INITIATED BY FUMING SULFURIC ACID AND PERCHLORIC ACID CATALYST SYSTEM
The yield of copolymerization of tetrahydrofuran and propylene oxide (THF:PO=100:5—15
by wt.) using a binary catalyst of fuming sulfuric acid (21% or 28%) and perchloric acid is around 50—60%
and the loss of THF in the reaction is below 10—15%. The average molecular weight of the product can be controlled in the range of 1000—2000 by varying the binary catalyst system. The present method
which is different from the usual copolymerization initiated by BF3-diol or SbCl5-diol system
shows the pecularities i.e.the yield of copolymerization with the low PO feed is not decreased
the hydroxyl funcitonality is equal to 2
and the end-groups are predominantly primary hydroxyls(around 65-70%).
Abstract
The yield of copolymerization of tetrahydrofuran and propylene oxide (THF:PO=100:5—15
by wt.) using a binary catalyst of fuming sulfuric acid (21% or 28%) and perchloric acid is around 50—60%
and the loss of THF in the reaction is below 10—15%. The average molecular weight of the product can be controlled in the range of 1000—2000 by varying the binary catalyst system. The present method
which is different from the usual copolymerization initiated by BF3-diol or SbCl5-diol system
shows the pecularities i.e.the yield of copolymerization with the low PO feed is not decreased
the hydroxyl funcitonality is equal to 2
and the end-groups are predominantly primary hydroxyls(around 65-70%).
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