$B:G=*99?7F|;~!'(B2017-05-20 20:59:01
$B$3$NJ,N`$G$h$/;H$o$l(B $B$F$$$k%-!<%o!<%I(B | $B%-!<%o!<%I(B | $B | |
---|---|---|---|
Packed Column Distillation | 1$B7o(B | ||
packed column | 1$B7o(B | ||
self-heat recuperation | 1$B7o(B | ||
Crude distillation unit | 1$B7o(B | ||
cryogenic separation | 1$B7o(B | ||
Energy saving | 1$B7o(B | ||
HTU | 1$B7o(B | ||
HETP | 1$B7o(B | ||
DWC | 1$B7o(B | ||
Mass Transfer | 1$B7o(B | ||
hydrogen purification | 1$B7o(B | ||
efficiency | 1$B7o(B |
$B | $B9V1iBjL\!?H/I=$B%-!<%o!<%I(B | $BH/I=7A<0(B | |
---|---|---|---|
4 | $B= | Mass Transfer Packed Column Distillation HTU | O |
6 | Energy Saving in a Crude Distillation Unit with a Divided Wall Column | Crude distillation unit Energy saving DWC | O |
210 | $B= | packed column HETP efficiency | O |
620 | $B%P%$%*%^%9%,%92=G3NAEECSH/EE%7%9%F%`$K$*$1$k3W?7E*$J?eAGJ,N%%W%m%;%9$N3+H/(B | hydrogen purification cryogenic separation self-heat recuperation | P |