<?xml version="1.0" encoding="UTF-8"?><xml><records><record><source-app name="Biblio" version="7.x">Drupal-Biblio</source-app><ref-type>17</ref-type><contributors><authors><author><style face="normal" font="default" size="100%">Sharma, Lohit</style></author><author><style face="normal" font="default" size="100%">Kiani, Daniyal</style></author><author><style face="normal" font="default" size="100%">Honer, Kenneth</style></author><author><style face="normal" font="default" size="100%">Baltrusaitis, Jonas</style></author></authors></contributors><titles><title><style face="normal" font="default" size="100%">Mechanochemical Synthesis of Ca- and Mg-Double Salt Crystalline Materials Using Insoluble Alkaline Earth Metal Bearing Minerals</style></title><secondary-title><style face="normal" font="default" size="100%">ACS Sustainable Chemistry &amp; Engineering</style></secondary-title><short-title><style face="normal" font="default" size="100%">ACS Sustainable Chem. Eng.</style></short-title></titles><dates><year><style  face="normal" font="default" size="100%">2019</style></year><pub-dates><date><style  face="normal" font="default" size="100%">2019/03/05</style></date></pub-dates></dates><urls><web-urls><url><style face="normal" font="default" size="100%">https://doi.org/10.1021/acssuschemeng.8b06129</style></url></web-urls></urls><publisher><style face="normal" font="default" size="100%">American Chemical Society</style></publisher><language><style face="normal" font="default" size="100%">eng</style></language><notes><style face="normal" font="default" size="100%">doi: 10.1021/acssuschemeng.8b06129</style></notes></record><record><source-app name="Biblio" version="7.x">Drupal-Biblio</source-app><ref-type>17</ref-type><contributors><authors><author><style face="normal" font="default" size="100%">Mazzei, Luca</style></author><author><style face="normal" font="default" size="100%">Broll, Valquiria</style></author><author><style face="normal" font="default" size="100%">Casali, Lucia</style></author><author><style face="normal" font="default" size="100%">Silva, Manoj</style></author><author><style face="normal" font="default" size="100%">Braga, Dario</style></author><author><style face="normal" font="default" size="100%">Grepioni, Fabrizia</style></author><author><style face="normal" font="default" size="100%">Baltrusaitis, Jonas</style></author><author><style face="normal" font="default" size="100%">Ciurli, Stefano</style></author></authors></contributors><titles><title><style face="normal" font="default" size="100%">Multifunctional Urea Cocrystal with Combined Ureolysis and Nitrification Inhibiting Capabilities for Enhanced Nitrogen Management</style></title><secondary-title><style face="normal" font="default" size="100%">ACS Sustainable Chemistry &amp; EngineeringACS Sustainable Chemistry &amp; Engineering</style></secondary-title><short-title><style face="normal" font="default" size="100%">ACS Sustainable Chem. Eng.</style></short-title></titles><dates><year><style  face="normal" font="default" size="100%">2019</style></year><pub-dates><date><style  face="normal" font="default" size="100%">2019/08/05</style></date></pub-dates></dates><urls><web-urls><url><style face="normal" font="default" size="100%">https://doi.org/10.1021/acssuschemeng.9b02607</style></url></web-urls></urls><publisher><style face="normal" font="default" size="100%">American Chemical Society</style></publisher><volume><style face="normal" font="default" size="100%">7</style></volume><pages><style face="normal" font="default" size="100%">13369 - 13378</style></pages><language><style face="normal" font="default" size="100%">eng</style></language><issue><style face="normal" font="default" size="100%">15</style></issue><notes><style face="normal" font="default" size="100%">doi: 10.1021/acssuschemeng.9b02607</style></notes></record><record><source-app name="Biblio" version="7.x">Drupal-Biblio</source-app><ref-type>17</ref-type><contributors><authors><author><style face="normal" font="default" size="100%">Zhu, Minghui</style></author><author><style face="normal" font="default" size="100%">Li, Bin</style></author><author><style face="normal" font="default" size="100%">Jehng, Jih-Mirn</style></author><author><style face="normal" font="default" size="100%">Sharma, Lohit</style></author><author><style face="normal" font="default" size="100%">Taborda, Julian</style></author><author><style face="normal" font="default" size="100%">Zhang, Lihua</style></author><author><style face="normal" font="default" size="100%">Stach, Eric</style></author><author><style face="normal" font="default" size="100%">Wachs, Israel E.</style></author><author><style face="normal" font="default" size="100%">Wu, Zili</style></author><author><style face="normal" font="default" size="100%">Baltrusaitis, Jonas</style></author></authors></contributors><titles><title><style face="normal" font="default" size="100%">Molecular structure and sour gas surface chemistry of supported K2O/WO3/Al2O3 catalysts</style></title><secondary-title><style face="normal" font="default" size="100%">Applied Catalysis B: Environmental</style></secondary-title><short-title><style face="normal" font="default" size="100%">Applied Catalysis B: Environmental</style></short-title></titles><keywords><keyword><style  face="normal" font="default" size="100%">Catalyst</style></keyword><keyword><style  face="normal" font="default" size="100%">CO</style></keyword><keyword><style  face="normal" font="default" size="100%">in situ</style></keyword><keyword><style  face="normal" font="default" size="100%">KO/WO/AlO</style></keyword><keyword><style  face="normal" font="default" size="100%">SO</style></keyword></keywords><dates><year><style  face="normal" font="default" size="100%">2018</style></year><pub-dates><date><style  face="normal" font="default" size="100%">2018/09/15/</style></date></pub-dates></dates><urls><web-urls><url><style face="normal" font="default" size="100%">http://www.sciencedirect.com/science/article/pii/S0926337318302443</style></url></web-urls></urls><volume><style face="normal" font="default" size="100%">232</style></volume><pages><style face="normal" font="default" size="100%">146 - 154</style></pages><isbn><style face="normal" font="default" size="100%">0926-3373</style></isbn><language><style face="normal" font="default" size="100%">eng</style></language></record><record><source-app name="Biblio" version="7.x">Drupal-Biblio</source-app><ref-type>17</ref-type><contributors><authors><author><style face="normal" font="default" size="100%">Honer, Kenneth</style></author><author><style face="normal" font="default" size="100%">Kalfaoglu, Eren</style></author><author><style face="normal" font="default" size="100%">Pico, Carlos</style></author><author><style face="normal" font="default" size="100%">McCann, Jane</style></author><author><style face="normal" font="default" size="100%">Baltrusaitis, Jonas</style></author></authors></contributors><titles><title><style face="normal" font="default" size="100%">Mechanosynthesis of Magnesium and Calcium Salt–Urea Ionic Cocrystal Fertilizer Materials for Improved Nitrogen Management</style></title><secondary-title><style face="normal" font="default" size="100%">ACS Sustainable Chemistry &amp; Engineering</style></secondary-title><short-title><style face="normal" font="default" size="100%">ACS Sustainable Chem. Eng.</style></short-title></titles><dates><year><style  face="normal" font="default" size="100%">2017</style></year><pub-dates><date><style  face="normal" font="default" size="100%">2017/10/02</style></date></pub-dates></dates><urls><web-urls><url><style face="normal" font="default" size="100%">http://dx.doi.org/10.1021/acssuschemeng.7b02621</style></url></web-urls></urls><publisher><style face="normal" font="default" size="100%">American Chemical Society</style></publisher><volume><style face="normal" font="default" size="100%">5</style></volume><pages><style face="normal" font="default" size="100%">8546 - 8550</style></pages><language><style face="normal" font="default" size="100%">eng</style></language><issue><style face="normal" font="default" size="100%">10</style></issue><notes><style face="normal" font="default" size="100%">doi: 10.1021/acssuschemeng.7b02621</style></notes></record><record><source-app name="Biblio" version="7.x">Drupal-Biblio</source-app><ref-type>17</ref-type><contributors><authors><author><style face="normal" font="default" size="100%">Taifan, William</style></author><author><style face="normal" font="default" size="100%">Baltrusaitis, Jonas</style></author></authors></contributors><titles><title><style face="normal" font="default" size="100%">Minireview: direct catalytic conversion of sour natural gas (CH4 + H2S + CO2) components to high value chemicals and fuels</style></title><secondary-title><style face="normal" font="default" size="100%">Catalysis Science &amp; Technology</style></secondary-title><short-title><style face="normal" font="default" size="100%">Catal. Sci. Technol.</style></short-title></titles><dates><year><style  face="normal" font="default" size="100%">2017</style></year><pub-dates><date><style  face="normal" font="default" size="100%">2017</style></date></pub-dates></dates><urls><web-urls><url><style face="normal" font="default" size="100%">http://dx.doi.org/10.1039/C7CY00272F</style></url></web-urls></urls><publisher><style face="normal" font="default" size="100%">The Royal Society of Chemistry</style></publisher><volume><style face="normal" font="default" size="100%">7</style></volume><pages><style face="normal" font="default" size="100%">2919 - 2929</style></pages><isbn><style face="normal" font="default" size="100%">2044-4753</style></isbn><language><style face="normal" font="default" size="100%">eng</style></language><abstract><style face="normal" font="default" size="100%">The abundance of natural gas reserves can facilitate the transition from fossil derived to fully renewable chemical and fuel generation. Natural gas, however, can contain more than 10% sour gas molecules (chiefly CO2 and H2S), especially in the Middle East and Russia. Currently, the most common sour natural gas separation technologies rely on the use of various amine-based absorption-desorption cycles in absorption towers, membrane separation and cryogenic processes. However, these processes are quite expensive and, unfortunately, result in the necessity for further processing of the sour gas stream. We feel that the implementation of catalytic activation of the sour gas stream, so as to form useful products, has been underexplored and thus has yet to be fully developed. In this paper, we present a series of catalytic reactions for the sour gas components so as to obtain useful chemicals or fuels, such as carbon disulfide (CS2), hydrogen (H2), ethylene (C2H4), ammonium sulfate ((NH4)2SO4) and ammonium thiosulfate ((NH4)2S2O3). Particular catalytic reactions which can form those products are (a) CH4 reforming with H2S on supported metal oxide catalysts, (b) CO2 + H2S + H2 catalytic reaction on K2O/WO3/Al2O3 to yield a CH3SH intermediate, (c) olefin production via CH3SH coupling on zeolites and supported metal oxides and (d) H2S + NH3 catalytic reaction to yield ammonium sulfate ((NH4)2SO4) and ammonium thiosulfate ((NH4)2S2O3) on partial oxidation catalysts. Thermodynamic considerations, together with catalyst design techniques, are discussed for each reaction.</style></abstract><issue><style face="normal" font="default" size="100%">14</style></issue></record><record><source-app name="Biblio" version="7.x">Drupal-Biblio</source-app><ref-type>17</ref-type><contributors><authors><author><style face="normal" font="default" size="100%">Mazeika, Romas</style></author><author><style face="normal" font="default" size="100%">Dambrauskas, Tadas</style></author><author><style face="normal" font="default" size="100%">Baltakys, Kestutis</style></author><author><style face="normal" font="default" size="100%">Mikolajunas, Marius</style></author><author><style face="normal" font="default" size="100%">Staugaitis, Gediminas</style></author><author><style face="normal" font="default" size="100%">Virzonis, Darius</style></author><author><style face="normal" font="default" size="100%">Baltrusaitis, Jonas.</style></author></authors></contributors><titles><title><style face="normal" font="default" size="100%">Molecular and Morphological Structure of Poultry Manure Derived Organo-Mineral Fertilizers (OMFs).</style></title><secondary-title><style face="normal" font="default" size="100%">ACS Sustainable Chemistry &amp; Engineering</style></secondary-title></titles><keywords><keyword><style  face="normal" font="default" size="100%">morphol poultry manure organomineral fertilizer</style></keyword></keywords><dates><year><style  face="normal" font="default" size="100%">2016</style></year><pub-dates><date><style  face="normal" font="default" size="100%">2016</style></date></pub-dates></dates><publisher><style face="normal" font="default" size="100%">American Chemical Society</style></publisher><volume><style face="normal" font="default" size="100%">4</style></volume><pages><style face="normal" font="default" size="100%">4788 - 4796</style></pages><isbn><style face="normal" font="default" size="100%">2168-0485</style></isbn><language><style face="normal" font="default" size="100%">eng</style></language><abstract><style face="normal" font="default" size="100%">In this work, we detd. the mol. and morphol. structures of complex granulated org. and organo-mineral fertilizers (OGFs and OMFs) obtained from poultry manure and mineral additives, such as diammonium phosphate (DAP) and potassium chloride (KCl).  XRD data indicated complex compns. of the mineral additives DAP and KCl, while OGF and OMF exhibited amorphous backgrounds with small peaks due to the common Earth crust minerals (Si, Mg, Zn, Ca).  Addn. of DAP generated several new chem. compds., while KCl did not react.  Thermogravimetric anal. indirectly showed mineral-mineral interactions at high temps., as can be inferred from their 478 °C peak shift.  Spatially resolved SEM-EDS anal. showed a particularly interesting colocalization of potassium, sulfur, and phosphorus within the OMF, suggesting a reactive salt interaction between DAP and minerals inherently present in OGF.  FTIR anal., on the other hand, did not show significant involvement of org. moieties with the interactions of mineral additives, suggesting org. compds. act mostly as inert support for DAP and KCl.  Collectively, these data suggest a complex nature of the OGF and OMF at the mol. and cryst. levels, which improves our understanding of these complex systems with direct relevance to sustainable nutrient management. [on SciFinder(R)]</style></abstract><issue><style face="normal" font="default" size="100%">9</style></issue><notes><style face="normal" font="default" size="100%">CAPLUS AN 2016:1191726(Journal; Online Computer File)</style></notes></record><record><source-app name="Biblio" version="7.x">Drupal-Biblio</source-app><ref-type>17</ref-type><contributors><authors><author><style face="normal" font="default" size="100%">Baltrusaitis, Jonas</style></author><author><style face="normal" font="default" size="100%">Luyben, William L.</style></author></authors></contributors><titles><title><style face="normal" font="default" size="100%">Methane Conversion to Syngas for Gas-to-Liquids (GTL): Is Sustainable CO2 Reuse via Dry Methane Reforming (DMR) Cost Competitive with SMR and ATR Processes?.</style></title><secondary-title><style face="normal" font="default" size="100%">ACS Sustainable Chemistry &amp; Engineering</style></secondary-title></titles><keywords><keyword><style  face="normal" font="default" size="100%">autothermal steam dry reforming competitive</style></keyword><keyword><style  face="normal" font="default" size="100%">methane conversion syngas liq sustainable carbon dioxide reuse</style></keyword></keywords><dates><year><style  face="normal" font="default" size="100%">2015</style></year></dates><publisher><style face="normal" font="default" size="100%">American Chemical Society</style></publisher><volume><style face="normal" font="default" size="100%">3</style></volume><pages><style face="normal" font="default" size="100%">2100 - 2111</style></pages><isbn><style face="normal" font="default" size="100%">2168-0485</style></isbn><language><style face="normal" font="default" size="100%">eng</style></language><abstract><style face="normal" font="default" size="100%">Carbon dioxide is a greenhouse gas and is obtained as a waste via burning various forms of fuels.  Syngas is an intermediate in large-scale long-chain hydrocarbon (C10-C20 alkanes and alcs.) prodn. processes via Fischer-Tropsch (FT) synthesis, typically to obtain high quality fuels.  Thus, it is of particular interest to engineer syngas prodn. processes for FT that can consume various combustion process waste CO2 in the process and thus partially contribute to the sustainable carbon neutral fuel synthesis.  In this work, a quant. economic comparison of five alternative processes is presented for the prodn. of synthesis gas with a hydrogen-to-carbon monoxide ratio of 2, which is suitable for feeding to the Fischer-Tropsch gas-to-liq. process.  Combinations of steam methane reforming (SMR), dry methane reforming (DMR), autothermal reforming (ATR) and reverse water gas shift (RWGS) are explored.  An amine absorber/stripper system is used for carbon dioxide removal.  The effects of the cost of natural gas and of liq. oxygen and the magnitude of a potential carbon tax are demonstrated.  With current prices of raw materials, the configuration with the lowest total annual cost (TAC) features a system composed of both SMR and DMR reactors. [on SciFinder(R)]</style></abstract><issue><style face="normal" font="default" size="100%">9</style></issue><notes><style face="normal" font="default" size="100%">CAPLUS AN 2015:1273933(Journal; Online Computer File)</style></notes></record><record><source-app name="Biblio" version="7.x">Drupal-Biblio</source-app><ref-type>17</ref-type><contributors><authors><author><style face="normal" font="default" size="100%">Krylova, V.</style></author><author><style face="normal" font="default" size="100%">Zalenkiene, S.</style></author><author><style face="normal" font="default" size="100%">Dukstiene, N.</style></author><author><style face="normal" font="default" size="100%">Baltrusaitis, J.</style></author></authors></contributors><titles><title><style face="normal" font="default" size="100%">Modification of polyamide-CdS-CdSe composite material films with Ag using cation-cation exchange reaction.</style></title><secondary-title><style face="normal" font="default" size="100%">Applied Surface Science</style></secondary-title></titles><keywords><keyword><style  face="normal" font="default" size="100%">exchange reaction</style></keyword><keyword><style  face="normal" font="default" size="100%">modification polyamide CdS CdSe composite material film Ag cation</style></keyword></keywords><dates><year><style  face="normal" font="default" size="100%">2015</style></year></dates><publisher><style face="normal" font="default" size="100%">Elsevier B.V.</style></publisher><volume><style face="normal" font="default" size="100%">351</style></volume><pages><style face="normal" font="default" size="100%">203 - 208</style></pages><isbn><style face="normal" font="default" size="100%">0169-4332</style></isbn><language><style face="normal" font="default" size="100%">eng</style></language><abstract><style face="normal" font="default" size="100%">Thin mixed CdSe-CdS-Ag2Se-Ag2S films were deposited on a polyamide 6 (PA) surface by successfully using a cation-exchange reaction between Cd2+ and Ag+ to convert CdSe-CdS into Ag2Se-Ag2S.  These were deposited using a K2SeS2O6 precursor soln. at 60 °C followed by cadmium acetate (Cd(CH3COO)2).  An aq. AgNO3 soln. was used as the Ag source.  XRD patterns showed a complex PA-Cd-S-Se-Ag film cryst. compn. with CdS, CdSe, Ag2S and Ag2Se peaks.  Calcd. dislocation d. ranged within 5-15 × 1013 lines·m-2 indicating high quality at. layers.  Atomic Absorption Spectroscopy (AAS) showed five- to ten-fold excess of chalcogens to metals in the thin films formed.  No chalcogenides were obsd. on the sample surface during XPS anal. after Ag exchange due to the desorption of CdS and CdSe layers, not diffused into the bulk of the polymer suggesting that silver chalcogenides were located subsurface, as opposed to the outermost layer, likely comprised of Ag2O. [on SciFinder(R)]</style></abstract><notes><style face="normal" font="default" size="100%">CAPLUS AN 2015:910421(Journal; Online Computer File)</style></notes></record></records></xml>