<?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%">Banerjee, Rahul</style></author></authors></contributors><titles><title><style face="normal" font="default" size="100%">Functionalized metal organic frameworks (MOFs) for reversible gas storage and sequestration applications</style></title><secondary-title><style face="normal" font="default" size="100%">Journal of the Indian Chemical Society</style></secondary-title></titles><keywords><keyword><style  face="normal" font="default" size="100%">carbon capture</style></keyword><keyword><style  face="normal" font="default" size="100%">CO2 adsorption</style></keyword><keyword><style  face="normal" font="default" size="100%">fluorination</style></keyword><keyword><style  face="normal" font="default" size="100%">Hydrogen storage</style></keyword><keyword><style  face="normal" font="default" size="100%">Metal-organic framework</style></keyword><keyword><style  face="normal" font="default" size="100%">structural isomerism</style></keyword></keywords><dates><year><style  face="normal" font="default" size="100%">2012</style></year><pub-dates><date><style  face="normal" font="default" size="100%">SEP</style></date></pub-dates></dates><number><style face="normal" font="default" size="100%">9</style></number><publisher><style face="normal" font="default" size="100%">SCIENTIFIC PUBL-INDIA</style></publisher><pub-location><style face="normal" font="default" size="100%">5-A, NEW PALI RD, PO BOX 91, NEAR HOTEL TAJ HARI MAHAL, JODHPUR, 342 003, INDIA</style></pub-location><volume><style face="normal" font="default" size="100%">89</style></volume><pages><style face="normal" font="default" size="100%">1197-1202</style></pages><language><style face="normal" font="default" size="100%">eng</style></language><abstract><style face="normal" font="default" size="100%">&lt;p&gt;The decreasing amount of fossil fuels and increasing threat of global warming from the pollutants have driven the search for clean energy source. Energy sources from fossil fuels still remain in the forefront despite being a major source of increased CO2 content in the atmosphere. Metal Organic Frameworks (MOFs) have emerged as promising materials for hydrogen storage and CO2 sequestration. Several factors influencing the hydrogen uptake of porous MOFs such as surface area, catenation, ligand functionalization, doping with alkali metals and unsaturated metal centers have been extensively studied. Similarly, well defined periodicity and tunable pore sizes along with less basic amino-functionalized MOFs enables them favorable for fast and reversible CO2 gas adsorption at low partial pressure and room temperature. In this review we present diverse aspects of metal organic frameworks like fluorination, amino functionalization for high hydrogen storage and CO2 sequestration capabilities.&lt;/p&gt;</style></abstract><issue><style face="normal" font="default" size="100%">9</style></issue><custom3><style face="normal" font="default" size="100%">Indian</style></custom3><custom4><style face="normal" font="default" size="100%">0.251
</style></custom4></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%">Gopalsamy, Karuppasamy</style></author><author><style face="normal" font="default" size="100%">Singh, Chandrodai Pratap</style></author><author><style face="normal" font="default" size="100%">Krishnamurty, Sailaja</style></author><author><style face="normal" font="default" size="100%">BabaRao, Ravichandar</style></author></authors></contributors><titles><title><style face="normal" font="default" size="100%">Metal-organic frameworks for enhanced hydrogen generation from syngas: a density functional theory approach</style></title><secondary-title><style face="normal" font="default" size="100%">CHEMPLUSCHEM</style></secondary-title></titles><keywords><keyword><style  face="normal" font="default" size="100%">carbon capture</style></keyword><keyword><style  face="normal" font="default" size="100%">H-2 separation</style></keyword><keyword><style  face="normal" font="default" size="100%">Metal organic</style></keyword><keyword><style  face="normal" font="default" size="100%">Porous coordination network (PCN-250)</style></keyword><keyword><style  face="normal" font="default" size="100%">Syngas</style></keyword></keywords><dates><year><style  face="normal" font="default" size="100%">2024</style></year><pub-dates><date><style  face="normal" font="default" size="100%">NOV</style></date></pub-dates></dates><volume><style face="normal" font="default" size="100%">89</style></volume><language><style face="normal" font="default" size="100%">eng</style></language><work-type><style face="normal" font="default" size="100%">Journal Article</style></work-type><custom3><style face="normal" font="default" size="100%">&lt;p&gt;Foreign&lt;/p&gt;
</style></custom3><custom4><style face="normal" font="default" size="100%">&lt;p&gt;3.4&lt;/p&gt;
</style></custom4></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%">Yang, Yutong</style></author><author><style face="normal" font="default" size="100%">Han, Yang</style></author><author><style face="normal" font="default" size="100%">Prasad, Babul</style></author><author><style face="normal" font="default" size="100%">Pang, Ruizhi</style></author><author><style face="normal" font="default" size="100%">Zou, Changlong</style></author><author><style face="normal" font="default" size="100%">Ho, W. S. Winston</style></author></authors></contributors><titles><title><style face="normal" font="default" size="100%">Carbon capture from flue gases using an integrated membrane skid</style></title><secondary-title><style face="normal" font="default" size="100%">Journal of Membrane Science</style></secondary-title></titles><keywords><keyword><style  face="normal" font="default" size="100%">Actual flue gas</style></keyword><keyword><style  face="normal" font="default" size="100%">carbon capture</style></keyword><keyword><style  face="normal" font="default" size="100%">Field trial</style></keyword><keyword><style  face="normal" font="default" size="100%">Integrated membrane skid</style></keyword><keyword><style  face="normal" font="default" size="100%">Membrane module</style></keyword></keywords><dates><year><style  face="normal" font="default" size="100%">2025</style></year><pub-dates><date><style  face="normal" font="default" size="100%">MAR</style></date></pub-dates></dates><volume><style face="normal" font="default" size="100%">718</style></volume><pages><style face="normal" font="default" size="100%">123674</style></pages><language><style face="normal" font="default" size="100%">eng</style></language><abstract><style face="normal" font="default" size="100%">&lt;p&gt;
	A prototype spiral-wound (SW) membrane module with a commercial-size diameter of 8 `' and a membrane area of 35 m(2) was fabricated using a new thin-film-composite facilitated transport membrane (FTM) scaled up to 21 `' in width by a continuous roll-to-roll coating process. This SW module was tested with an actual coal flue gas at the Center for Applied Energy Research (CAER) at the University of Kentucky, which exhibited an average CO2 permeance of 4269 GPU with a CO2/N-2 selectivity of 165 and remained stable for 100 h. The permeance and selectivity results are consistent with those determined from lab and scale-up flat-sheet samples. An integrated membrane skid was then constructed, where 2 SW membrane modules were arranged to form an enriching cascade. The 8 `'-diameter prototype SW module previously tested at CAER was installed as the primary CO2 capture stage, while a smaller SW module (5 `' diameter and 12 m(2) membrane area) was used to further enrich the CO2 to &amp;gt;95% purity. By using a simulated coal flue gas (13% CO2), the skid was operated at steady-state for 800 h with 91.0% of the CO2 removed from the flue gas, delivering 1.33 tonne/day CO2 product at 95.5% dry purity. The bench skid was then installed at the National Carbon Capture Center (NCCC), Wilsonville, AL and tested with an actual natural gas (NG) flue gas (8.6% CO2). 90-99% CO2 capture degrees were demonstrated during the parametric testing, and the skid was operated at steady state for 500 h cumulatively with 91.0% CO2 capture and &amp;gt;95% CO2 purity. A simulated natural gas combined cycle (NGCC) flue gas (4.3% CO2) slipstream was further provided by diluting the NG flue gas with air, and 90-99% CO2 capture degrees were also achieved with dry CO2 purities all above 95%. All these capture degrees and CO2 purities were in good agreement with their model predictions.&lt;/p&gt;
</style></abstract><work-type><style face="normal" font="default" size="100%">Article</style></work-type><custom3><style face="normal" font="default" size="100%">&lt;p&gt;
	Foreign&lt;/p&gt;
</style></custom3><custom4><style face="normal" font="default" size="100%">&lt;p&gt;
	8.4&lt;/p&gt;
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