FITM Vapor Pressure of Butane Questions

The questions are:

2: 28,31,32,34,35,37,44,36

Those are on the excel and papers.

Part 2

Thermostart/Butane plot+calusius-clapeyron Fit -File

Butane Antoine Fit-File

Ethane Plot +Clausius -Clapeyron Fit- File

Propane Antoine Fit+Clausius-Clapeyron -File

Ethane Antoine Fit-File

Propane Antoine Fit- File

those are on Datafit

Vapor Pressure of Butane
5
log P = (-1.31 + 0.01)*(1000/T) + (7.61 + 0.06)
4
log P, P in mm Hg
3
2
1
0
-1
-2
-3
0
1
2
3
4
5
1000/Temperature (K-1)
6
7
8
Vapor Pressure of Butane
5
log (Pressure, P, in mm Hg)
4
3
log P = (-1.31 + 0.01)*1000/T + (7.61 + 0.06)
2
1
0
-1
-2
-3
2
3
4
5
1000/Temperature, K-1
6
7
8
Carbon dioxide
Temperature (K)
Carbon Dioxide
Pressure (MPa)
1000/Temperature (K-1)
Temperature (oC)
Carbon Dioxide
Pressure (mm Hg)
216.58
5.182E-01
4.617
-57
3886
221.58
6.402E-01
4.513
-52
4802
226.58
7.826E-01
4.413
-47
5870
231.58
9.475E-01
4.318
-42
7107
236.58
1.137E+00
4.227
-37
8527
241.58
1.353E+00
4.139
-32
10147
246.58
1.598E+00
4.055
-27
11983
251.58
1.874E+00
3.975
-22
14054
256.58
2.183E+00
3.897
-17
16376
261.58
2.529E+00
3.823
-12
18968
266.58
2.913E+00
3.751
-7
21849
271.58
3.338E+00
3.682
-2
25040
276.58
3.808E+00
3.616
3
28562
281.58
4.325E+00
3.551
8
32436
286.58
4.892E+00
3.489
13
36692
291.58
5.514E+00
3.430
18
41358
296.58
6.197E+00
3.372
23
46481
301.58
6.951E+00
3.316
28
52133
Butane
log (CO2 Pressure)
Temperature
(K)
Butane
Pressure
(MPa)
Temperature (oC)
Butane Pressure
(mm Hg)
log
(Butane
Pressure)
3.59
134.86
6.737E-07
7.415
-138
0.005053
-2.30
3.68
139.86
3.77
144.86
1.679E-06
7.150
-133
0.012595
-1.90
3.902E-06
6.903
-128
0.029269
3.85
-1.53
149.86
8.514E-06
6.673
-123
0.063861
-1.19
3.93
154.86
1.755E-05
6.457
-118
0.131658
-0.88
4.01
159.86
3.438E-05
6.255
-113
0.257894
-0.59
4.08
164.86
6.431E-05
6.066
-108
0.482365
-0.32
4.15
169.86
1.154E-04
5.887
-103
0.865196
-0.06
4.21
174.86
1.992E-04
5.719
-98
1.494048
0.17
4.28
179.86
3.323E-04
5.560
-93
2.492155
0.40
4.34
184.86
5.370E-04
5.409
-88
4.027681
0.61
4.40
189.86
8.431E-04
5.267
-83
6.323695
0.80
4.46
194.86
1.289E-03
5.132
-78
9.669045
0.99
4.51
199.86
1.924E-03
5.004
-73
14.427436
1.16
4.56
204.86
2.807E-03
4.881
-68
21.051231
1.32
4.62
209.86
4.011E-03
4.765
-63
30.085724
1.48
4.67
214.86
5.624E-03
4.654
-58
42.182719
1.63
4.72
219.86
7.747E-03
4.548
-53
58.106528
1.76
224.86
1.050E-02
4.447
-48
78.741475
1.90
229.86
1.401E-02
4.350
-43
105.083642
2.02
234.86
1.844E-02
4.258
-38
138.273871
2.14
239.86
2.394E-02
4.169
-33
179.564767
2.25
244.86
3.071E-02
4.084
-28
230.343943
2.36
249.86
3.895E-02
4.002
-23
292.119023
2.47
254.86
4.887E-02
3.924
-18
366.517641
2.56
259.86
6.070E-02
3.848
-13
455.302443
2.66
264.86
7.470E-02
3.776
-8
560.318579
2.75
269.86
9.113E-02
3.706
-3
683.553713
2.83
274.86
1.103E-01
3.638
2
827.093018
2.92
279.86
1.324E-01
3.573
7
993.006662
3.00
284.86
1.578E-01
3.510
12
1183.747348
3.07
289.86
1.869E-01
3.450
17
1401.490254
3.15
294.86
2.198E-01
3.391
22
1648.635579
3.22
299.86
2.570E-01
3.335
27
1927.808537
3.29
304.86
2.988E-01
3.280
32
2241.484333
3.35
309.86
3.456E-01
3.227
37
2592.363188
3.41
314.86
3.977E-01
3.176
42
2982.995312
3.47
319.86
4.555E-01
3.126
47
3416.155934
3.53
324.86
5.193E-01
3.078
52
3894.695287
3.59
329.86
5.895E-01
3.032
57
4421.463607
3.65
334.86
6.665E-01
2.986
62
4999.311128
3.70
339.86
7.508E-01
2.942
67
5631.313101
3.75
344.86
8.427E-01
2.900
72
6320.394769
3.80
349.86
9.426E-01
2.858
77
7069.781396
3.85
354.86
1.051E+00
2.818
82
7882.398224
3.90
359.86
1.168E+00
2.779
87
8762.220577
3.94
364.86
1.295E+00
2.741
92
9712.548729
3.99
1000/Temperature
-1
(K )
369.86
1.431E+00
2.704
97
10736.382926
4.03
374.86
1.578E+00
2.668
102
11837.473476
4.07
379.86
1.736E+00
2.633
107
13021.070812
4.11
384.86
1.905E+00
2.598
112
14290.175179
4.16
389.86
2.087E+00
2.565
117
15650.787071
4.19
394.86
2.281E+00
2.533
122
17107.406859
4.23
399.86
2.489E+00
2.501
127
18666.035036
4.27
404.86
2.711E+00
2.470
132
20333.422156
4.31
409.86
2.949E+00
2.440
137
22119.319023
4.34
414.86
3.204E+00
2.410
142
24033.476437
4.38
419.86
3.479E+00
2.382
147
26092.395756
4.42
424.86
3.777E+00
2.354
152
28330.579817
4.45
Isobutane
Temperature
(K)
Isobutane
Pressure
(MPa)
113.55
1.936E-08
118.55
123.55
Pro
Temperature (oC)
Isobutane Pressure
(mm Hg)
log
(Isobutane
Pressure)
Temperature
(K)
Propane
Pressure
(MPa)
8.807
-160
0.000145
-3.84
85.87
1.980E-10
6.776E-08
8.435
-155
0.000508
-3.29
90.87
1.327E-09
2.122E-07
8.094
-150
0.001592
-2.80
95.87
7.180E-09
128.55
6.029E-07
7.779
-145
0.004522
-2.34
100.87
3.241E-08
133.55
1.571E-06
7.488
-140
0.011782
-1.93
105.87
1.254E-07
138.55
3.791E-06
7.218
-135
0.028437
-1.55
110.87
4.244E-07
143.55
8.547E-06
6.966
-130
0.064106
-1.19
115.87
1.281E-06
148.55
1.813E-05
6.732
-125
0.135956
-0.87
120.87
3.495E-06
153.55
3.639E-05
6.513
-120
0.272947
-0.56
125.87
8.734E-06
158.55
6.954E-05
6.307
-115
0.521555
-0.28
130.87
2.020E-05
163.55
1.271E-04
6.114
-110
0.953028
-0.02
135.87
4.363E-05
168.55
2.230E-04
5.933
-105
1.672413
0.22
140.87
8.864E-05
173.55
3.771E-04
5.762
-100
2.828708
0.45
145.87
1.706E-04
178.55
6.168E-04
5.601
-95
4.626530
0.67
150.87
3.126E-04
183.55
9.784E-04
5.448
-90
7.338453
0.87
155.87
5.485E-04
188.55
1.509E-03
5.304
-85
11.317681
1.05
160.87
9.249E-04
193.55
2.268E-03
5.167
-80
17.011399
1.23
165.87
1.505E-03
198.55
3.329E-03
5.037
-75
24.971054
1.40
170.87
2.371E-03
203.55
4.782E-03
4.913
-70
35.864949
1.55
175.87
3.627E-03
208.55
6.731E-03
4.795
-65
50.487402
1.70
180.87
5.403E-03
213.55
9.301E-03
4.683
-60
69.763237
1.84
185.87
7.852E-03
218.55
1.263E-02
4.576
-55
94.762793
1.98
190.87
1.116E-02
223.55
1.689E-02
4.473
-50
126.677918
2.10
195.87
1.554E-02
228.55
2.225E-02
4.375
-45
166.873723
2.22
200.87
2.124E-02
233.55
2.891E-02
4.282
-40
216.835332
2.34
205.87
2.852E-02
238.55
3.709E-02
4.192
-35
278.190377
2.44
210.87
3.770E-02
243.55
4.702E-02
4.106
-30
352.701505
2.55
215.87
4.911E-02
248.55
5.896E-02
4.023
-25
442.258870
2.65
220.87
6.311E-02
253.55
7.318E-02
3.944
-20
548.880138
2.74
225.87
8.009E-02
258.55
8.995E-02
3.868
-15
674.680484
2.83
230.87
1.005E-01
263.55
1.096E-01
3.794
-10
821.917592
2.91
235.87
1.247E-01
268.55
1.324E-01
3.724
-5
992.856649
3.00
240.87
1.531E-01
273.55
1.587E-01
3.656
0
1189.972860
3.08
245.87
1.864E-01
278.55
1.888E-01
3.590
5
1415.816432
3.15
250.87
2.249E-01
283.55
2.230E-01
3.527
10
1672.787565
3.22
255.87
2.692E-01
288.55
2.618E-01
3.466
15
1963.736491
3.29
260.87
3.198E-01
293.55
3.055E-01
3.407
20
2291.213422
3.36
265.87
3.773E-01
298.55
3.544E-01
3.350
25
2658.068591
3.42
270.87
4.421E-01
303.55
4.089E-01
3.294
30
3067.077227
3.49
275.87
5.149E-01
308.55
4.695E-01
3.241
35
3521.164569
3.55
280.87
5.963E-01
313.55
5.364E-01
3.189
40
4023.255860
3.60
285.87
6.868E-01
318.55
6.101E-01
3.139
45
4576.351345
3.66
290.87
7.871E-01
323.55
6.911E-01
3.091
50
5183.526277
3.71
295.87
8.978E-01
328.55
7.797E-01
3.044
55
5847.930915
3.77
300.87
1.019E+00
333.55
8.763E-01
2.998
60
6572.940538
3.82
305.87
1.153E+00
338.55
9.815E-01
2.954
65
7361.780410
3.87
310.87
1.298E+00
343.55
1.096E+00
2.911
70
8217.675796
3.91
315.87
1.457E+00
1000/Temperature
-1
(K )
348.55
1.219E+00
2.869
75
9145.502097
3.96
320.87
1.630E+00
353.55
1.353E+00
2.828
80
10147.584505
4.01
325.87
1.816E+00
358.55
1.497E+00
2.789
85
11228.423390
4.05
330.87
2.019E+00
363.55
1.652E+00
2.751
90
12393.269183
4.09
335.87
2.237E+00
368.55
1.819E+00
2.713
95
13645.872193
4.14
340.87
2.473E+00
373.55
1.999E+00
2.677
100
14991.482852
4.18
345.87
2.727E+00
378.55
2.191E+00
2.642
105
16436.101653
4.22
350.87
3.000E+00
383.55
2.398E+00
2.607
110
17985.729090
4.25
355.87
3.294E+00
388.55
2.620E+00
2.574
115
19647.865778
4.29
360.87
3.611E+00
393.55
2.857E+00
2.541
120
21430.012337
4.33
365.87
3.953E+00
398.55
3.112E+00
2.509
125
23343.419689
4.37
403.55
3.387E+00
2.478
130
25400.838885
4.40
Propane
Ethane
1000/Temperature (K- Temperature
1
(oC)
)
Propane
Pressure (mm
Hg)
log
(Propane
Pressure)
Temperature
(K)
Ethane
Pressure
(MPa)
1000/Temperature (K-
Temperature
1
)
(oC)
11.646
-187
0.000001
-5.83
90.352
1.13E-06
11.068
-183
11.005
-182
0.000010
-5.00
95.352
3.93E-06
10.487
-178
10.431
-177
0.000054
-4.27
100.35
1.19E-05
9.965
-173
9.914
-172
0.000243
-3.61
105.35
3.23E-05
9.492
-168
9.446
-167
0.000940
-3.03
110.35
7.93E-05
9.062
-163
9.020
-162
0.003184
-2.50
115.35
0.00017847
8.669
-158
8.630
-157
0.009605
-2.02
120.35
0.00037266
8.309
-153
8.273
-152
0.026214
-1.58
125.35
0.00072896
7.978
-148
7.945
-147
0.065513
-1.18
130.35
0.0013464
7.672
-143
7.641
-142
0.151520
-0.82
135.35
0.0023639
7.388
-138
7.360
-137
0.327222
-0.49
140.35
0.0039684
7.125
-133
7.099
-132
0.664877
-0.18
145.35
0.0064014
6.880
-128
6.855
-127
1.279455
0.11
150.35
0.0099651
6.651
-123
6.628
-122
2.344918
0.37
155.35
0.015026
6.437
-118
6.416
-117
4.113713
0.61
160.35
0.022018
6.236
-113
6.216
-112
6.937321
0.84
165.35
0.031442
6.048
-108
6.029
-107
11.289178
1.05
170.35
0.043867
5.870
-103
5.852
-102
17.784713
1.25
175.35
0.059926
5.703
-98
5.686
-97
27.207737
1.43
180.35
0.08031
5.545
-93
5.529
-92
40.522832
1.61
185.35
0.10577
5.395
-88
5.380
-87
58.896343
1.77
190.35
0.13711
5.253
-83
5.239
-82
83.706884
1.92
195.35
0.17518
5.119
-78
5.105
-77
116.559585
2.07
200.35
0.22086
4.991
-73
4.978
-72
159.283099
2.20
205.35
0.27509
4.870
-68
4.857
-67
213.925093
2.33
210.35
0.33882
4.754
-63
4.742
-62
282.788256
2.45
215.35
0.41305
4.644
-58
4.632
-57
368.355292
2.57
220.35
0.49878
4.538
-53
4.528
-52
473.348927
2.68
225.35
0.59706
4.438
-48
4.427
-47
600.686899
2.78
230.35
0.70894
4.341
-43
4.331
-42
753.436960
2.88
235.35
0.83551
4.249
-38
4.240
-37
934.951887
2.97
240.35
0.97788
4.161
-33
4.152
-32
1148.644461
3.06
245.35
1.1372
4.076
-28
4.067
-27
1398.114977
3.15
250.35
1.3146
3.994
-23
3.986
-22
1686.963731
3.23
255.35
1.5113
3.916
-18
3.908
-17
2019.241056
3.31
260.35
1.7285
3.841
-13
3.833
-12
2398.772267
3.38
265.35
1.9676
3.769
-8
3.761
-7
2829.682704
3.45
270.35
2.23
3.699
-3
3.692
-2
3316.097705
3.52
275.35
2.5171
3.632
2
3.625
3
3862.367629
3.59
280.35
2.8305
3.567
7
3.560
8
4472.767826
3.65
285.35
3.1721
3.504
12
3.498
13
5151.723661
3.71
290.35
3.5439
3.444
17
3.438
18
5903.810511
3.77
295.35
3.9483
3.386
22
3.380
23
6733.753763
3.83
300.35
4.3888
3.329
27
3.324
28
7646.128793
3.88
3.269
33
8645.961017
3.94
3.217
38
9738.800888
3.99
3.166
43
10928.398717
4.04
3.117
48
12222.255120
4.09
3.069
53
13624.120405
4.13
3.022
58
15141.495189
4.18
2.977
63
16780.379965
4.22
2.934
68
18548.275352
4.27
2.891
73
20451.931902
4.31
2.850
78
22501.850481
4.35
2.810
83
24707.781890
4.39
2.771
88
27083.977301
4.43
2.733
93
29649.938317
4.47
Ethane
log (Ethane
Pressure (mm
Pressure)
Hg)
0.008482
-2.07
0.029489
-1.53
0.089610
-1.05
0.242630
-0.62
0.594904
-0.23
1.338635
0.13
2.795180
0.45
5.467650
0.74
10.098830
1.00
17.730708
1.25
29.765448
1.47
48.014449
1.68
74.744397
1.87
112.704268
2.05
165.148581
2.22
235.834394
2.37
329.029558
2.52
449.481964
2.65
602.374537
2.78
793.340242
2.90
1028.409573
3.01
1313.958056
3.12
1656.586232
3.22
2063.344683
3.31
2541.358993
3.41
3098.129780
3.49
3741.157661
3.57
4478.318283
3.65
5317.487293
3.73
6266.840365
3.80
7334.703183
3.87
8529.701456
3.93
9860.310881
3.99
11335.682211
4.05
12964.816186
4.11
14758.213669
4.17
16726.375524
4.22
18879.802615
4.28
21230.495929
4.33
23792.706637
4.38
26581.435973
4.42
29614.685418
4.47
32918.707131
4.52
2:321
…
تفاصيل المهمة
=
CHE1102: Intro to Chm Eng 2, Spring 2021, Sect. 01
and see the instructions associated with Homework
3. To solve the problems in Polymath, use the NLE
function. Click the f(x) = button to enter the
equation. Insert a range to search for answers.
Realize that the answers to #1 will be between -5
and 5, the answer to #1 will be between 0 and 1, and
the answer to #3 will be between 0 and 0.1999 (If
you get an answer of roughly 0.9, then you found a
. (.root that would result in a negative mole fraction
Job 4: Copy and paste the results from the
sphericaltankdepth.xls file to a new file, edit the
function in columns C, E, and G to be consistent with
problems 1, 2, and 3 (in three separate worksheets).
Put in new initial guesses that are based off of what
.you saw in Polymath for the prior problem
Job 5: Put in the functions for problems 1, 2, and 3
into the edited worksheets, and solve via Newton’s
.method
Job 6: Lastly, do problem 6 on p. 53 (with further
explanation on p. 54) of the PowerPoint file. You
may want to see p. 84 of the PowerPoint file for this
one, too. Your answer should be
watergasshiftequilbrium.xls. Although not asked for,
you could do this for one case in Polymath and get
.watergasshift.pol
إرسال المهمة
< Next Previous 22 DOO םםם علبة الوارد الإعلامات قائمة مهام التقويم لوحة المعلومات 2:32 1 ... تفاصيل المهمة CHE1102: Intro to Chm Eng 2, Spring 2021, Sect. 01 .now this page :For the entire HW set Open coursepacks12withaudio.pptx and sphericaltankdepth.xls from Canvas/Files. Realize that sphericaltankdepth.xls is the answer. Your job, probably in another worksheet within the same file, should be to reproduce it using the following instructions in Jobs 1 and 2 Job 1: Listen to coursepacks12withaudio.pptx pp. .53-70 Job 2: Reproduce sphericaltankdepth.xls using pp. 60-70 of the PowerPoint file. This is problem 5 on p. 53 of coursepacks12withaudio.pptx. Send those .results to me not done already Job 3: Solve problems 1, 2, and 3 on p. 53 of coursepacks12withaudio.pptx using Polymath. If you have a Mac, use either Parallel Desktop or Amazon Web Services just like you did for DataFit, and see the instructions associated with Homework 3. To solve the problems in Polymath, use the NLE function. Click the f(x) = button to enter the equation. Insert a range to search for answers. Realize that the answers to #1 will be between -5 and 5, the answer to #1 will be between 0 and 1, and the answer to #3 will be between 0 and 0.1999 (If vou get an answer of roughlv 09 then vou found a = إرسال المهمة < Next Previous 22 DOO םםם علبة الوارد الإعلامات قائمة مهام التقويم لوحة المعلومات