TY - JOUR
T1 - Catalytic reduction of N-nitrosodimethylamine with nanophase nickel-boron
AU - Frierdich, Andrew J.
AU - Joseph, Claire E.
AU - Strathmann, Timothy J.
N1 - Funding Information:
This work was supported by the National Science Foundation through WaterCAMPWS, a Science and Technology Center of Advanced Materials for the Purification of Water with Systems (CTS-0120978) and funding provided by the Division of Chemical, Bioengineering, Environmental, and Transport Systems (CBET 07-46453 CAREER). XRD, XPS, TEM, and SEM analyses were performed at the Center for Microanalysis of Materials, University of Illinois, which is partially supported by the U.S. Department of Energy under grant DEFG02-91-ER45439. Experimental assistance and valuable insights were provided by John Shapley, Charles Werth, Tias Paul, Kathryn Guy, Rick Haasch, Jim Mabon, Mauro Sardela (Univ. Illinois), and two anonymous reviewers.
PY - 2009/7/25
Y1 - 2009/7/25
N2 - Recent work by the authors shows that toxic N-nitrosamines, widely detected in disinfected wastewater and drinking water and recalcitrant towards conventional treatment processes, can be rapidly reduced to less hazardous products by treatment with hydrogen and Raney nickel catalysts. Unfortunately, Raney Ni catalysts are pyrophoric when dry and are readily deactivated when exposed to air, severely limiting their application for water treatment. In this work, a non-pyrophoric and air-tolerant nickel-boron (NiB) catalyst is described, and its reactivity with N-nitrosodimethylamine (NDMA) is quantified. The catalyst, prepared by aqueous reduction of NiCl2 with NaBH4, has an elemental composition of 85 wt.% Ni and 7 wt.% B. Nanophase primary catalyst particles are formed and aggregate in micrometer-sized assemblies in solution. The catalyst has a specific surface area of 18 m2 g-1, and the surface contains Ni(0) and B in a mixture of oxidation states (0/+III). Kinetic studies show that NDMA is rapidly reduced via hydrogenation to dimethylamine and ammonia in H2(g)-saturated (PH2 = 1 atm) aqueous NiB suspensions, with mass- and surface area-normalized first-order rate constants of 29.5 ± 2.4 L gNi-1 h-1 and 1.38 ± 0.11 L mcat-2 h-1, respectively. Although the mass-normalized rate constant is less than that measured for Raney Ni, the surface area-normalized rate constant is greater, suggesting higher intrinsic reactivity of the NiB surface if the availability of surface sites for NDMA reactions on either catalyst surface is not significantly affected by aggregation of the catalyst nanoparticles. Kinetic studies show that reactivity of the NiB catalyst with NDMA is unaffected by solution pH and extended pre-exposure of the dry catalyst to air (Raney Ni is immediately deactivated by exposure to air). The NiB catalyst is also more tolerant of dissolved oxygen and low concentrations of dissolved (bi)sulfide than Raney Ni, suggesting potential for greater catalyst longevity during water treatment applications.
AB - Recent work by the authors shows that toxic N-nitrosamines, widely detected in disinfected wastewater and drinking water and recalcitrant towards conventional treatment processes, can be rapidly reduced to less hazardous products by treatment with hydrogen and Raney nickel catalysts. Unfortunately, Raney Ni catalysts are pyrophoric when dry and are readily deactivated when exposed to air, severely limiting their application for water treatment. In this work, a non-pyrophoric and air-tolerant nickel-boron (NiB) catalyst is described, and its reactivity with N-nitrosodimethylamine (NDMA) is quantified. The catalyst, prepared by aqueous reduction of NiCl2 with NaBH4, has an elemental composition of 85 wt.% Ni and 7 wt.% B. Nanophase primary catalyst particles are formed and aggregate in micrometer-sized assemblies in solution. The catalyst has a specific surface area of 18 m2 g-1, and the surface contains Ni(0) and B in a mixture of oxidation states (0/+III). Kinetic studies show that NDMA is rapidly reduced via hydrogenation to dimethylamine and ammonia in H2(g)-saturated (PH2 = 1 atm) aqueous NiB suspensions, with mass- and surface area-normalized first-order rate constants of 29.5 ± 2.4 L gNi-1 h-1 and 1.38 ± 0.11 L mcat-2 h-1, respectively. Although the mass-normalized rate constant is less than that measured for Raney Ni, the surface area-normalized rate constant is greater, suggesting higher intrinsic reactivity of the NiB surface if the availability of surface sites for NDMA reactions on either catalyst surface is not significantly affected by aggregation of the catalyst nanoparticles. Kinetic studies show that reactivity of the NiB catalyst with NDMA is unaffected by solution pH and extended pre-exposure of the dry catalyst to air (Raney Ni is immediately deactivated by exposure to air). The NiB catalyst is also more tolerant of dissolved oxygen and low concentrations of dissolved (bi)sulfide than Raney Ni, suggesting potential for greater catalyst longevity during water treatment applications.
KW - Disinfection byproducts
KW - Hydrogenation
KW - NDMA
KW - Nickel-boron
KW - Water treatment
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U2 - 10.1016/j.apcatb.2009.03.007
DO - 10.1016/j.apcatb.2009.03.007
M3 - Article
AN - SCOPUS:66049096487
SN - 0926-3373
VL - 90
SP - 175
EP - 183
JO - Applied Catalysis B: Environmental
JF - Applied Catalysis B: Environmental
IS - 1-2
ER -