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Dear experts, in the MRC hybrid refrigeration LNG liquefaction process, for the MRC hybrid refrigerant system, how is the total amount of refrigerant calculated? The five components of the refrigerant are nitrogen, methane, ethylene, propane, and isobutane. I would appreciate it if someone could guide me through the calculation process. Thank you!
To calculate the total amount of refrigerant in an MRC mixed refrigerant system, it is first necessary to understand the proportions of each component within the system, as well as the physical and thermodynamic properties of those components. The following are the basic calculation steps: 1. Determine the mass ratio or molar ratio of each component. This is usually determined based on the process design document or experimental data. 2. Obtain or measure relevant physical properties of each component, such as density (ρ, in units of kg/m³) and specific heat capacity (Cp, in units of kJ/kg·K). These values can be found in standard material handbooks, or estimated using relevant software. 3. Calculate the mass of each component. If the total cooling capacity required by the system, Q (in kJ), is known, the masses of each component can be allocated according to their respective contributions to cooling. The calculation formula is: \ where \( m_i \) is the mass of the i-th component, and \( \Delta T_i \) is the temperature difference provided by that component. 4. The total mass of the MRC mixed refrigerant system can be obtained by summing the masses of each component calculated as follows: \ where \( m_{total} \) is the total mass of the refrigerant, and \( m_i \) is the mass of each component. 5. Finally, verify whether the calculation results meet the system’s operating conditions and safety standards. Please adjust the above steps and calculation methods according to the actual process parameters and design requirements. For more accurate calculations, it may be necessary to use specialized software or consult professional chemical/refrigeration engineers for analysis. .