 Experienced in PSA based hydrogen gas production plant employing M/S LINDE AG, GERMANY technology to meet the growing hydrogen need in petroleum refineries. The hydrogen gas plant is designed to produce 5*181TPD with purity of 99.9% hydrogen gas.  Feed stock: Refinery fuel gas. Natural gas,LPG and Naphtha or any combination of above gases. Each trains have Feed preparation unit, feed hydrodesuphurization, steam hydrocarbon reforming with waste heat recovery system,HT shift converter and Pressure Swing Adsorption unit (PSA) Feed preparation - To preheat and compress or pump the feed gas/liquid for HDS.  HDS - To remove sulphur content from the feed gas in the form of H2S CoMox,ZnO is catalyst  Steam Reforming- 288 no’s of tubes,84 no’s of burners, top fired furnace,Balanced draft furnace having ID/FD fan, alkalized/ non alkalized NiO Catalyst, COT:867degree celcius.To produce syn gas by feed gas react with steam. HT shift converter - TO convert CO to CO2 water gas shift reaction catalyst - Fe2O3 PSA unit - 12 adsorbers adsorbents: activated alumina,activated charcoal,and molecular sieve to remove CO,CO2,CH4 and H2O produce 99.9%hydrogen.

 Experienced in Ammonia plant employing ICI revamped KBR process, for help to produce 1320MTPD ammonia. The process steps are feed desulfurization, primary reforming,process air compression, secondary reformer, carbon monoxide shift conversion, carbon dioxide removal,methanation,syn gas compression,ammonia synthesis,ammonia refrigeration,ammonia and hydrogen recovery and ammonia storage & refrigeration. Primary reformer - 264 no’s of tubes,90 no’s of burners, top fired furnace,Balanced draft furnace having turbine driven ID/FD fan, alkalized/ non alkalized NiO Catalyst, COT:760degree celcius. Secondary reformer - To Introduce process air in the process its help to reduce the methane content and nitrogen for ammonia production COT: 920degree celcius process operations of CO2 removal unit; process operations of ammonia synthesis loop and ammonia recovery,