Feasibility Study and New Proposal for Oil Removal
نویسندگان
1 Department of Physics and Chemistry, Tashkent Institute of Irrigation and Agricultural Mechanization Engineers, National Research University, Tashkent, Uzbekistan.
2 University of Tashkent for Applied Sciences, Str. Gavhar 1, Tashkent 100149, Uzbekistan
3 Tashkent Institute of Irrigation and Agricultural Mechanization Engineers, National Research University, Tashkent, Uzbekistan
4 Baku Eurasian University, Baku, AZ 1073, Azerbaijan
5 Department of Digital Economy, Samarkand State University Named after Sharof Rashidov, University Boulevard, 15, Samarkand, 703004, Uzbekistan
6 Western Caspian University, Scientific Researcher, Baku, Azerbaijan
7 Department of Audit, Tashkent State University of Economics, Tashkent, Uzbekistan
8 Department of Finance, Termez State University, Uzbekistan
9 Kimyo International University in Tashkent, Uzbekistan
10 Department of Zoology, Human Morphophysiology and Nutrition (PhD), Nukus State Pedagogical Institute Named after Ajiniyaz., Uzbekistan
doi
10.48309/chemm.2025.506325.1901چکیده
One of the problems with refining gasoline complexes is the high speed of corrosion. This is due to the higher amount of water and chlorine in the hydrogen outlet from the catalyst recovery vessel. Chlorine and water exist together with various hydrocarbons produce oil. Green oil is an oligomer found in refineries in all C2, C3, and C4 hydrocarbon reactors. It is a combination of C2 and C20 unsaturated and other active elements along with water and chlorine. In the present study, the removal of this substance in the hydrogen gas from the reclaiming chamber of the Naphtha treatment plant with continuous revival is investigated. Design of chlorine adsorbent container is one of the most important strengths of this study. By taking action, one of the main problems of the catalytic conversion units in French and American companies has been resolved. According to the best results to achieve maximum efficiency of gasoline product with octane number 95: catalyst circulating flow 800 kg/hr, 5.5 Barg pressure of the gas compressor output, 0.95 wt% catalyst chloride concentration, 261 °C temperature, 0.37% A volume of benzene is produced that calculates the catalytic, conversion unit mass efficiency of 96% wt and the volumetric efficiency of 88%, Under these conditions, coke formed 3.64%, purity of circulating hydrogen gas equal to 94%, H2/HC molar ratio of 2.7.
