This online calculation program can calculate the size of vertical gas-liquid two-phase separator, and can choose the situation with or without demister.Sizing and calculation for a vertical gas liquid separator with or without Mesh Pad
The online calculation program of horizontal gas-liquid two-phase separator is based on Souders Brown formula to design and calculate the size of horizontal gas-liquid separator with or without demister. K value can be obtained by GPSA method, droplet size method and user input.
This online calculation program (online calculation program for volume of separator at different liquid levels) is used to calculate the volume (volume) of vertical separator and horizontal separator at different liquid levels.Users can select different head types: ellipsoidal head, spherical head, flat head, ASME F&D head.After the data is changed, the diagram is also
Reference: HG/T 20570-95 Engineering Design Regulations for Process System P11, where LN 'is the distance between inlet and outlet nozzles, m;DT 'is the diameter of horizontal vessel, m;A is the height of gas space, m;VG is the gas flow, m3/h;ρL is the liquid density, kg/m3;ρG is the gas density, kg/m3
Reference standard: HG/T 20570-95 Process System Engineering Design Regulations P9Calculate according to the formulaWhere, DT is the diameter of the cylindrical part, m;LT is the length of the cylindrical part, m;VL is the liquid volume flow, m3/h;T is the retention time, min;C=LT/DT=2-4 (2.5 recommended);A is the variable liquid surface
Reference: HG/T 20570-95 Process System Engineering Design Regulations P8 is calculated according to the formula HL=VLt/(47.1D2), where HL is the liquid height of vertical separator, m2;T is the retention time, min;D is the diameter of the container, m;VL is the liquid volume flow, m3/h
Reference standard: HG/T 20570-95 Specification for Engineering Design of Process Systems P7 is calculated according to the formula, where d * is the droplet diameter, m;ρL is the liquid density, kg/m3;ρG is the gas density, kg/m3;CW is the resistance coefficient;Vt is the floating (settling) velocity, m/s;g=9.8m/s2
Bibliography: HG/T 20507-95 Regulations on Engineering Design of Process Systems P6 is calculated according to the formula, where KS is a constant;ρG is the gas density, kg/m3;ρL is the liquid density, kg/m3;Vt is the floating (settling) velocity, m/s
Reference data: P16 in SY/T 0515-2007 Specification for Separators is calculated according to the formula W=1440V/t, where W is the liquid treatment capacity under flowing conditions, m3/d;V -- liquid settling volume, m3;T -- retention time, min
The natural gas processing capacity of the separator can be calculated by the modified Stokes law.When Stokes theorem is adopted, the processing capacity shall be based on the principle of the minimum droplet size settled in the moving airflow at a given speed.Under operating conditions, the maximum operating apparent speed of the gas is
Reference: Q/HS 300-2003 Specification for Design and Manufacture of Oil Gas Separator P19 (16) is calculated according to the formula, where K is a constant, usually 0.107;ρG is the gas density, kg/m3;ρL is the droplet density, kg/m3;UG is the gas flow rate of the free cross sectional area of the mist eliminator of the oil-gas separator, m/s
Bibliography: Calculation of Pressure Drop of Axial Flow Cyclone Separator according to the formula △ P=ζρV2/2, where,ζIs the pressure loss coefficient;ρIs the gas density, kg/m3;V is the gas velocity, m/s
