Page 5 of 6
ACS Catalysis
The manuscript was written through contributions of all authors. /
Given the faster hydrolysis, we examined the pH dependence
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All authors have given approval to the final version of the manuꢀ
script.
of the reaction rate at 0.5 µmole catalyst loading (vs. 1.5
µmole for UiOꢀ66). As shown in Figures S3–S4 and Table S1
(see ESI), and like the behavior with UiOꢀ66, the UiOꢀ67ꢀ
catalyzed hydrolysis rate increases with decreasing pH, yieldꢀ
ing an apparent rate constant essentially identical to that for
UiOꢀ66 (but at oneꢀthird the loading of UiOꢀ66).55 Furtherꢀ
more, although it is has been reported that UiOꢀ67 is unstable
in water, in our hands, UiOꢀ67 showed no such instability.60
Figures S5ꢀS6 in the ESI shows the powder Xꢀray diffractoꢀ
grams and nitrogen sorption isotherms of UiOꢀ67 preꢀ and
postꢀcatalysis. The diffractograms look identical to one anothꢀ
er and the decrease in surface area (2300 m2/g to 1020 m2/g) is
attributed to pore clogging from the hydrolysis products; simiꢀ
lar decreases in surface area have been observed for phosphate
modified Zr6ꢀbased nodes.61,62 Furthermore, filtration of the
MOF midꢀcatalysis ceased the catalytic reaction. In addition,
inductively coupled plasma mass spectrometry of the superꢀ
nate showed no evidence of leached zirconium. Thus, the acꢀ
tive catalyst is UiOꢀ67.
Funding Sources
O.K.F. and J.T.H. gratefully acknowledge DTRA for financial
support (grant HDTRAꢀ1ꢀ10ꢀ0023).
SUPPORTING INFORMATION
Supporting Information Available: Uncatalyzed reaction rate and
pH dependence, hydrolysis rate and pH dependence using UiOꢀ
67, powder xꢀray diffractograms and surface area analysis of UiOꢀ
67 pre/post catalysis, and potentiometric titration of UiOꢀ67. This
material is available free of charge via the Internet at
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AUTHOR INFORMATION
Corresponding Author
* j-hupp@u.northwestern.edu; o-
farha@northwestern.edu;
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