چکیده مقاله
The experimental data of an industrial unit producing sodium chloride salt by recrystallization method with evaporative crystallization equipped with a thermo compressor TC were investigated The feasibility of replacing the proposed double effect evaporation DEE model instead of the current plan was modeled The findings indicate that maintaining an equal amount of motive steam in both modes results in a 44% increase in production within the DEE model Furthermore, concurrent with the production increase, there will be a reduction of 60 units in the specific consumption of natural gas fuel per ton of product produced In the existing unit, due to the presence of a TC in the path of steam entering the heat exchanger, high pressure steam is needed, which in the studied industrial unit is 10 bar; in contrast, within the proposed DEE model, the motive steam pressure is 2 bar, as a result, approximately 1 8% less fuel will be required in the boiler to generate every ton of steam These results demonstrate the potential for significant efficiency gains and reduced resource utilization by implementing the DEE plan within the sodium chloride salt production process
کلیدواژهها
نویسندگان
Manouchehr Manouchehrianfard
Utility supervisor of ISM Company, Iran Salts Mining Company, Garmsar, Iran,
Farhad Mahmoudiyekta
Manager of ISM Company, Iran Salts Mining Company, Garmsar, Iran,
Ali Aghamohsenifashmi
Planning Manager of ISM Company, Iran Salts Mining Company, Garmsar, Iran
Bita Soleimani
Faculty of Chemical, Petroleum and Gas Engineering, Semnan University, Semnan, Iran
شیوه ارجاع
Manouchehrianfard, Manouchehr and Mahmoudiyekta, Farhad and Aghamohsenifashmi, Ali and Soleimani, Bita,1402,Investigation of double effect evaporation model to energy consuming reduction in NaCl production process: industrial case,The 16th International Conference on Innovation and Research in Engineering Sciences
ارائهشده در
مجموعه مقالات شانزدهمین کنفرانس بین المللی نوآوری و تحقیق در علوم مهندسی19 آبان 1402