钢铁酸洗机组的废盐酸再生利用——蒸发分离法

aspenone · 发表于 1970-1-1 08:00:00

本帖最后由 aspenone 于 2015-6-29 01:13 编辑

QQ图片20150629010050.png

1 2 3 4 5 6 7 8 9
B1 B2 B6 B3 B4 B5  B1
  B1 B2 B2 B3 B4 B4 B5 B6
LIQUID MIXED VAPOR LIQUID LIQUID LIQUID LIQUID LIQUID LIQUID
Substream: MIXED
摩尔流量 kmol/hr
  HCL                   1.25813E-8 41.00919 41.00919 1.43260E-9 2.03257E-9 2.00552E-9 2.7043E-11 2.00547E-9 41.00919
  FECL2                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  H2O                      347.4188 549.4114 339.5305 209.8809 163.1542 160.9835 2.170746 160.9835 339.5305
  FE++                      11.83410 23.13782       0.0 23.13782 11.45615 11.30373 .1524226 11.30373       0.0
  H3O+                      41.14025 9.850604       0.0 9.850606 9.850606 9.719545 .1310611 9.719545       0.0
  FECL2(S)                      0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  SALT1                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  SALT2                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  OH-                   1.5306E-15 1.1825E-12       0.0 1.1825E-12 9.8459E-15 9.7149E-15 1.3100E-16 9.7157E-15       0.0
  CL-                      64.80845 56.12622       0.0 56.12622 32.76288 32.32697 .4359059 32.32697       0.0
摩尔分率
  HCL                   2.7045E-11 .0603488 .1077659 4.7914E-12 9.3570E-12 9.3570E-12 9.3570E-12 9.3567E-12 .1077659
  FECL2                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  H2O                      .7468134 .8085105 .8922341 .7019532 .7510879 .7510879 .7510879 .7510879 .8922341
  FE++                      .0254386 .0340494       0.0 .0773851 .0527389 .0527389 .0527389 .0527389       0.0
  H3O+                      .0884353 .0144960       0.0 .0329456 .0453477 .0453477 .0453477 .0453477       0.0
  FECL2(S)                      0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  SALT1                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  SALT2                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  OH-                   3.2902E-18 1.7401E-15       0.0 3.9548E-15 4.5326E-17 4.5326E-17 4.5326E-17 4.5330E-17       0.0
  CL-                      .1393126 .0825950       0.0 .1877159 .1508254 .1508254 .1508254 .1508254       0.0
质量流量 kg/hr
  HCL                   4.58721E-7 1495.221 1495.221 5.22335E-8 7.41087E-8 7.31227E-8 9.8601E-10 7.31205E-8 1495.221
  FECL2                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  H2O                      6258.847 9897.801 6116.738 3781.063 2939.269 2900.162 39.10659 2900.162 6116.738
  FE++                      660.8857 1292.153       0.0 1292.153 639.7791 631.2669 8.512180 631.2669       0.0
  H3O+                      782.5975 187.3848       0.0 187.3848 187.3848 184.8917 2.493131 184.8917       0.0
  FECL2(S)                      0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  SALT1                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  SALT2                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  OH-                   2.6032E-14 2.0111E-11       0.0 2.0111E-11 1.6746E-13 1.6523E-13 2.2280E-15 1.6524E-13       0.0
  CL-                      2297.670 1989.857       0.0 1989.857 1161.551 1146.096 15.45428 1146.096       0.0
质量分率
  HCL                   4.5872E-11 .1006042 .1964306 7.2042E-12 1.5038E-11 1.5038E-11 1.5038E-11 1.5038E-11 .1964306
  FECL2                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  H2O                      .6258847 .6659617 .8035694 .5214930 .5964445 .5964445 .5964445 .5964445 .8035694
  FE++                      .0660885 .0869409       0.0 .1782167 .1298257 .1298257 .1298258 .1298257       0.0
  H3O+                      .0782597 .0126079       0.0 .0258445 .0380246 .0380246 .0380246 .0380246       0.0
  FECL2(S)                      0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  SALT1                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  SALT2                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  OH-                   2.6032E-18 1.3532E-15       0.0 2.7738E-15 3.3981E-17 3.3981E-17 3.3981E-17 3.3984E-17       0.0
  CL-                      .2297670 .1338852       0.0 .2744457 .2357051 .2357051 .2357051 .2357051       0.0
总流量    kmol/hr       465.2016 679.5353 380.5397 298.9955 217.2238 214.3337 2.890135 214.3337 380.5397
总流量    kg/hr          10000.00 14862.42 7611.959 7250.457 4927.983 4862.417 65.56619 4862.417 7611.959
总流量    l/min          134.3075 2.00242E+5 2.00163E+5 79.07872 58.52395 57.74530 .7786537 57.74530 116.6646
温度       K             313.1500 386.9281 386.9281 386.9281 318.1500 318.1500 318.1499 318.1500 318.1500
压力       atm             1.000000 1.000000 1.000000 1.000000 1.000000 .9997533 .9997533 1.000000 1.000000
Vapor Frac                      0.0 .5600000 1.000000       0.0       0.0       0.0       0.0       0.0       0.0
液相分率                   1.000000 .4400000       0.0 1.000000 1.000000 1.000000 1.000000 1.000000 1.000000
固相分率                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
焓       cal/mol       -62694.01  -54867.47  -53252.16  -56923.31  -60912.51  -60912.51  -60912.51  -60912.51  -64998.07
焓       cal/gm       -2916.535  -2508.635  -2662.201  -2347.413  -2685.003  -2685.003  -2685.003  -2685.003  -3249.406
焓       cal/sec       -8.1015E+6 -1.0357E+7 -5.6290E+6 -4.7277E+6 -3.6755E+6 -3.6266E+6  -48901.50 -3.6266E+6 -6.8707E+6
熵       cal/mol-K    -35.82811  -16.12032  -6.461401  -28.41350  -34.27804  -34.27791  -34.27792  -34.27804  -36.82603
熵       cal/gm-K       -1.666729  -.7370489  -.3230206  -1.171720  -1.510964  -1.510959  -1.510959  -1.510964  -1.841020
密度       mol/cc          .0577284 5.65594E-5 3.16858E-5 .0630164 .0618618 .0618618 .0618618 .0618618 .0543637
密度       gm/cc          1.240934 1.23704E-3 6.33813E-4 1.528110 1.403409 1.403409 1.403409 1.403409 1.087442
平均分子量                21.49606 21.87144 20.00306 24.24938 22.68620 22.68620 22.68620 22.68620 20.00306
60F 液相体积 l/min             138.7481          138.7481
Substream: $TOTAL
总流量    kg/hr          10000.00 14862.42 7611.959 7250.457 7250.457 4862.417 2388.041 4862.417 7611.959
焓       cal/sec       -8.1015E+6 -1.0357E+7 -5.6290E+6 -4.7277E+6 -4.8755E+6 -3.6266E+6 -1.2490E+6 -3.6266E+6 -6.8707E+6
Substream: CISOLID
摩尔流量 kmol/hr
  HCL                            0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  FECL2                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  H2O                            0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  FE++                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  H3O+                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  FECL2(S)                      0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  SALT1                         0.0       0.0       0.0       0.0 11.68167       0.0 11.68167       0.0       0.0
  SALT2                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  OH-                            0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  CL-                            0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
摩尔分率
  HCL                            0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  FECL2                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  H2O                            0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  FE++                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  H3O+                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  FECL2(S)                      0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  SALT1                         0.0       0.0       0.0       0.0 1.000000       0.0 1.000000       0.0       0.0
  SALT2                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  OH-                            0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  CL-                            0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
质量流量 kg/hr
  HCL                            0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  FECL2                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  H2O                            0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  FE++                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  H3O+                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  FECL2(S)                      0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  SALT1                         0.0       0.0       0.0       0.0 2322.475       0.0 2322.475       0.0       0.0
  SALT2                         0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  OH-                            0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
  CL-                            0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0       0.0
质量分率
  HCL                                  0.0       0.0
  FECL2                                  0.0       0.0
  H2O                                  0.0       0.0
  FE++                                  0.0       0.0
  H3O+                                  0.0       0.0
  FECL2(S)                               0.0       0.0
  SALT1                            1.000000    1.000000
  SALT2                                  0.0       0.0
  OH-                                  0.0       0.0
  CL-                                  0.0       0.0
总流量    kmol/hr             0.0       0.0       0.0       0.0 11.68167       0.0 11.68167       0.0       0.0
总流量    kg/hr                0.0       0.0       0.0       0.0 2322.475       0.0 2322.475       0.0       0.0
总流量    l/min                0.0       0.0       0.0       0.0 20.05556       0.0 20.05556       0.0       0.0
温度       K                      318.1500    318.1499
压力       atm             1.000000 1.000000 1.000000 1.000000 1.000000 .9997533 .9997533 1.000000 1.000000
Vapor Frac                               0.0       0.0
液相分率                               0.0       0.0
固相分率                            1.000000    1.000000
焓       cal/mol             -3.6983E+5 -3.6983E+5
焓       cal/gm                -1860.162 -1860.162
焓       cal/sec             -1.2001E+6 -1.2001E+6
熵       cal/mol-K             -1240.424 -1240.424
熵       cal/gm-K             -6.239133 -6.239133
密度       mol/cc                9.70776E-3 9.70776E-3
密度       gm/cc                   1.930034    1.930034
平均分子量                         198.8135    198.8135
60F 液相体积

素问 · 发表于 1970-1-1 08:00:00

钢铁酸洗机组的废盐酸再生利用——蒸发分离法

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