PRO/II模拟浮阀塔出现问题

shanzhapi · 发表于 2016-4-14 10:16:54

PRO/II模拟一个直径1600mm的浮阀塔，结果如下：
TRAY  VAPOR  LIQUID  VLOAD -- DESIGN -- NEXT SMALLER NEXT LARGER NP
      M3/S M3/S M3/S DIA, MM  FF DIA, MM  FF DIA, MM  FF
  ----  ----- -------  ----- ------- ---- ------- ---- ------- ---- --
2 1.167 0.00002  0.035 911.5  50.4 762. 72.1 914. 50.1 1
  MECHANICAL RESTRICTION ON TRAY 2,  FOR FF = 60.0, CALCD. DIA =  835.3
3 1.150 0.00002  0.034 907.2  50.3 762. 71.4 914. 49.6 1
  MECHANICAL RESTRICTION ON TRAY 3,  FOR FF = 60.0, CALCD. DIA =  831.0
4 1.133 0.00002  0.034 903.0  50.3 762. 70.6 914. 49.1 1
  MECHANICAL RESTRICTION ON TRAY 4,  FOR FF = 60.0, CALCD. DIA =  826.8
5 1.116 0.00002  0.034 898.8  50.3 762. 69.9 914. 48.6 1
  MECHANICAL RESTRICTION ON TRAY 5,  FOR FF = 60.0, CALCD. DIA =  822.6
6 1.100 0.00002  0.034 894.6  50.2 762. 69.2 914. 48.1 1
  MECHANICAL RESTRICTION ON TRAY 6,  FOR FF = 60.0, CALCD. DIA =  818.4
7 1.084 0.00001  0.033 890.5  50.2 762. 68.5 914. 47.6 1
  MECHANICAL RESTRICTION ON TRAY 7,  FOR FF = 60.0, CALCD. DIA =  814.3
8 1.069 0.00001  0.033 886.4  50.1 762. 67.8 914. 47.1 1
  MECHANICAL RESTRICTION ON TRAY 8,  FOR FF = 60.0, CALCD. DIA =  810.2
9 1.993 0.00574  0.062 1249.5  60.0 1219. 62.8 1372. 50.5 1
10 1.994 0.00578  0.063 1253.3  60.0 1219. 63.2 1372. 50.7 1
11 1.984 0.00580  0.063 1253.6  60.0 1219. 63.2 1372. 50.8 1
12 1.972 0.00582  0.063 1253.2  60.0 1219. 63.2 1372. 50.7 1
13 1.960 0.00584  0.063 1252.8  60.0 1219. 63.1 1372. 50.7 1
14 1.949 0.00585  0.063 1252.6  60.0 1219. 63.1 1372. 50.7 1
15 1.939 0.00587  0.063 1252.8  60.0 1219. 63.1 1372. 50.7 1
16 1.930 0.00590  0.064 1253.3  60.0 1219. 63.2 1372. 50.8 1
17 1.920 0.00592  0.064 1254.0  60.0 1219. 63.2 1372. 50.8 1
18 1.899 0.00594  0.063 1251.0  60.0 1219. 63.0 1372. 50.6 1
** WARNING **  Design diameter includes mechanical restriction allowances.
如何处理？
浮阀塔使用PRO/II模拟时不用输入塔径？

[求助] PRO/II模拟浮阀塔出现问题