Chemistry Reference
In-Depth Information
ϰ͘Ϭ
^ŝůŝĐŽŶĞͲƉŽůLJĞƐƚĞƌ
ŝƐŝůŽdžĂŶĞͲƉŽůLJƚĞƐƚĞƌ
ϯ͘ϱ
ϯ͘Ϭ
Ϯ͘ϱ
Ϯ͘Ϭ
ϭ͘ϱ
ϭ͘Ϭ
Ϭ͘ϱ
Ϭ͘Ϭ
ϯϱ ϱϬ ϲϬ ϳϬ ϴϬ ϵϬ ϭϬϬ ϭϬ ϭϮϬ ϯϬ ϭϰϬ ϱϬ ϭϲϬ
dĞŵƉĞƌĂƚƵƌĞ; Ϳ
Fig. 6.2 The change in the apparent rate constant (h −1 ) with increasing temperature. Two differ-
ent acyl acceptors were used, one derived from a disiloxane ( white bars ) and the other from a
polysiloxane ( grey bars ). Each bar is the average of three independent trials; error bars indicate
the standard deviation
6.4
Elongation Kinetics
Polyester synthesis is a second order process [ 18 ]. The rate of polymer elongation
can be determined using a plot of the average degree of polymerization (DP avg ) ver-
sus time, where DP avg = 1/(1 − p ) in which p is the extent of monomer conversion.
The slope of the line can be taken as the apparent rate of polymer elongation. Mono-
mer conversion was determined using the integration values from 1 H NMR that
correspond to the O -methylene protons of the diol before and after esterification.
6.4.1
CPr-TMDS and 3HP-TMDS
When polyesterifications were performed in the temperature range 35-70 °C, the
rate of polymer elongation was slow (Fig. 6.2 ). Increases in temperature to 100 °C,
increased the polymerization rate to 1.94 h −1 . This increase is attributed to the in-
creasing proficiency of the enzyme coupled with the ease of removal of the meth-
anol by-product. It was hypothesized that temperatures above 100 °C would be
deleterious to the functioning of the enzyme as a result of thermal denaturation.
However, this was not the case (see Sect. 6.7). In fact the apparent rate constant
Search WWH ::




Custom Search