Temperature ℃ 33。4374 48。8391 101。2220

Pressure Mpa 0。3000 0。3000 0。3000

VaEGr Frac 0。046278 1。0000 0。0000

Mole Flow kmol/h 7987。0830 709。7589 7277。3252

Mass Flow kg/h 235376。6076 34909。8083 200467。0000

MassFrac/ EG 0。08722825 0。5795649 0。001491498

Hydrogen Peroxid 3226。9409 0。000000 3226。9403

Propene 14230。3904 14230。3904 0。0000

1,2-Propylene Ox 20531。4883 20232。5001 298。9958

Water 44010。2887 382。1425 43628。1478

1,2-Propanediol 1616。2920 0。0000 1616。2920

Methanol 151700。0000 3。5644 151696。4697

Oxygen 61。2135 61。2135 0。0000

Nitrogen 0。000000 0。000000 0。000000

Tatal/kg 235376。6076 235376。8083

表3-3  EG反应器2物衡表

进  料 出  料

Temperature ℃ 35。0000 35。0000

Pressure Mpa 1。50000 1。5000

VaEGr Frac 0。0000 0。0000

Mole Flow kmol/h 7445。8375 7442。5179

Mass Flow kg/h 207104。7905 207104。7055

MassFrac/ EG 2。37511e-011 0。02527439

Hydrogen Peroxid 3226。9401 0。0000

Propene 7000。0022 3047。7764

1,2-Propylene Ox 0。0000 5234。4453

Water 44010。1363 45650。8331

1,2-Propanediol 1616。2920 1905。0521

Methanol 151251。4247 151251。4247

Oxygen 年产20万吨乙二醇反应器设计(3):http://www.youerw.com/huaxue/lunwen_97955.html