Mô phỏng công nghệ hóa học và dầu khí - Dynamic modeling using unisim design

Nhóm Mô phỏng Công nghệ Hoá học và Dầu khí Trường Đại học Bách khoa Hà Nội Dynamic Modeling using UniSim Design Unit 1 Getting Started in Steady State New case 2 Tab Fluid pkgs PR Name Oil & Gas Plant Components Nitrogen CO2 Methane Ethane Propane i-butane n-butane i-pentane n-pentane n-hexane H2O New case 3 Fluid Pkgs 4 Fluid Pkgs: PR 5 Fluid Pkgs: Rename 6 Components 7 Hypocomponent Heavier 8 Name NBP Liq Density NBP200 93.3oC NBP280 138oC NBP425 218oC NBP630 332oC NBP920 493oC 961 kg/m3 Hypocomponent Heavier 9 Hypocomponent Heavier 10 Enter Simulation Environment Adding Streams 11 Specs Alpha Bravo Charlie Temperature, oC 88 80 49 Pressure, kPa 6480 6650 6620 Flow Rate, kmole/h 10900 9980 11800 Adding a Stream Alpha 12 Adding a Stream Bravo 13 Adding a Stream Charlie 14 Adding a Stream Alpha Components Mol Fraction Components Mol Fraction N2 0.0150 n-Pentane 0.0050 CO2 0.0230 n-Hexane 0.0060 Methane 0.7590 H2O 0.0380 Ethane 0.0660 NPB200* 0.0070 Propane 0.0340 NBP280* 0.0140 i-Butane 0.0060 NBP425* 0.0060 n-Butane 0.0130 NBP630* 0.0030 i-Pentane 0.0040 NBP920* 0.0010 15 Adding a Stream Alpha 16 Adding a Stream Bravo Components Mol Fraction Components Mol Fraction N2 0.0050 n-Pentane 0.0190 CO2 0.0100 n-Hexane 0.0100 Methane 0.7190 H2O 0.0400 Ethane 0.0620 NPB200* 0.0100 Propane 0.0410 NBP280* 0.0210 i-Butane 0.0100 NBP425* 0.0100 n-Butane 0.0260 NBP630* 0.0050 i-Pentane 0.0100 NBP920* 0.0020 17 Adding a Stream Charlie Components Mol Fraction Components Mol Fraction N2 0.0170 n-Pentane 0.0060 CO2 0.0260 n-Hexane 0.0070 Methane 0.7300 H2O 0.0430 Ethane 0.0740 NPB200* 0.0080 Propane 0.0390 NBP280* 0.0160 i-Butane 0.0060 NBP425* 0.0060 n-Butane 0.0140 NBP630* 0.0030 i-Pentane 0.0040 NBP920* 0.0010 18 Save your case!  Save your case as 01.FS.usc 19 Add a Mixer 20 In this cell... Enter Inlets Alpha Bravo Charlie Outlet To Sep Add a Mixer 21 Add a Mixer 22 Add a Separator 23 Name HP Sep Inlet stream To Sep Vapour Otlet Stream HP Vap Liquid Outlet Stream HP Liq Add a Separator 24 Add a Separator 25 Add a Cooler 26 Name E-100 Inlet stream HP Vap Outlet Stream Hot Vap Enegy Stream Qe-100 Parameters Delta P 70 kPa Worksheet Hot Vap temperature 27oC Add a Cooler 27 Add a Valve 28 Name VLV-100 Inlet stream HP liq Outlet stream HP liq1 Worksheet HP liq1 pressure 260 kPa Add a Valve 29 Save as 01.SS.usc 30