Group | Sigma | Epsilon / kB | Charge |
---|---|---|---|
C | 2.757 Å | 28.129 K | +0.6512 e |
O | 3.033 Å | 80.507 K | -0.3256 e |
Temperature | Rho L (sim) | Rho L (exp) | Rho G (sim) | Rho G (exp) |
---|---|---|---|---|
(K) | (Kg m-3) | (Kg m-3) | (Kg m-3) | (Kg m-3) |
228 | 1133 ± 10 | 1134.9 | 23.0 ± 3.1 | 21.8 |
238 | 1084 ± 7 | 1094.9 | 29.4 ± 2.4 | 31.2 |
248 | 1045 ± 11 | 1052.6 | 44.3 ± 3.0 | 43.7 |
258 | 997.2 ± 13 | 1006.1 | 56.8 ± 4.9 | 60.2 |
268 | 949.6 ± 7.9 | 956.5 | 83.7 ± 5.3 | 82.4 |
278 | 879.5 ± 15.3 | 898.5 | 110.9 ± 10.7 | 114.7 |
288 | 801.4 ± 41.7 | 824.4 | 152.5 ± 7.5 | 160.7 |
Temperature | Pressure (sim) | Pressure (exp) |
---|---|---|
(K) | (bar) | (bar) |
228 | 9.0 ± 1.2 | 8.2 |
238 | 12.2 ± 0.9 | 11.9 |
248 | 18.5 ± 1.1 | 16.6 |
258 | 23.7 ± 1.5 | 22.6 |
268 | 32.7 ± 1.8 | 30.1 |
278 | 41.3 ± 1.9 | 39.2 |
288 | 53.4 ± 2.2 | 50.2 |
Temperature | Liquid Phase | Vapor Phase |
---|---|---|
228 | Liquid Phase | Vapor Phase |
238 | Liquid Phase | Vapor Phase |
248 | Liquid Phase | Vapor Phase |
258 | Liquid Phase | Vapor Phase |
268 | Liquid Phase | Vapor Phase |
278 | Liquid Phase | Vapor Phase |
288 | Liquid Phase | Vapor Phase |
Temperature | File |
---|---|
228 | excel_228 |
238 | excel_238 |
248 | excel_248 |
258 | excel_258 |
268 | excel_268 |
278 | excel_278 |
288 | excel_288 |
File Type | Equil A | Equil B | Equil C | Prod A | Prod B |
---|---|---|---|---|---|
Input | in - eqa | in - eqb | in - eqc | in - pra | in - prb |
Results | res - eqa | res - eqb | res - eqc | res - pra | res - prb |
Plots | plots - eqa | plots - eqb | plots - eqc | plots - pra | plots - prb |
Output Conf. | xyz - eqa | xyz - eqb | xyz - eqc | xyz - pra | xyz - prb |
File Type | Equil A | Equil B | Prod A | Prod B |
---|---|---|---|---|
Input | in - eqa | in - eqb | in - pra | in - prb |
Results | res - eqa | res - eqb | res - pra | res - prb |
Plots | plots - eqa | plots - eqb | plots - pra | plots - prb |
Output Conf. | xyz - eqa | xyz - eqb | xyz - pra | xyz - prb |
File Type | Equil A | Equil B | Prod A | Prod B | Prod C |
---|---|---|---|---|---|
Input | in - eqa | in - eqb | in - pra | in - prb | in - prc |
Results | res - eqa | res - eqb | res - pra | res - prb | res - prc |
Plots | plots - eqa | plots - eqb | plots - pra | plots - prb | plots - prc |
Output Conf. | xyz - eqa | xyz - eqb | xyz - pra | xyz - prb | xyz - prc |
File Type | Equil A | Equil B | Prod A | Prod B | Prod C |
---|---|---|---|---|---|
Input | in - eqa | in - eqb | in - pra | in - prb | in - prc |
Results | res - eqa | res - eqb | res - pra | res - prb | res - prc |
Plots | plots - eqa | plots - eqb | plots - pra | plots - prb | plots - prc |
Output Conf. | xyz - eqa | xyz - eqb | xyz - pra | xyz - prb | xyz - prc |
File Type | Equil A | Equil B | Prod A | Prod B | Prod C |
---|---|---|---|---|---|
Input | in - eqa | in - eqb | in - pra | in - prb | in - prc |
Results | res - eqa | res - eqb | res - pra | res - prb | res - prc |
Plots | plots - eqa | plots - eqb | plots - pra | plots - prb | plots - prc |
Output Conf. | xyz - eqa | xyz - eqb | xyz - pra | xyz - prb | xyz - prc |
File Type | Equil A | Equil B | Equil C | Prod A | Prod B | Prod C | Prod D |
---|---|---|---|---|---|---|---|
Input | in - eqa | in - eqb | in - eqc | in - pra | in - prb | in - prc | in - prd |
Results | res - eqa | res - eqb | res - eqc | res - pra | res - prb | res - prc | res - prd |
Plots | plots - eqa | plots - eqb | plots - eqc | plots - pra | plots - prb | plots - prc | plots - prd |
Output Conf. | xyz - eqa | xyz - eqb | xyz - eqc | xyz - pra | xyz - prb | xyz - prc | xyz - prd |
File Type | Equil A | Equil B | Equil C | Prod A | Prod B | Prod C | Prod D |
---|---|---|---|---|---|---|---|
Input | in - eqa | in - eqb | in - eqc | in - pra | in - prb | in - prc | in - prd |
Results | res - eqa | res - eqb | res - eqc | res - pra | res - prb | res - prc | res - prd |
Plots | plots - eqa | plots - eqb | plots - eqc | plots - pra | plots - prb | plots - prc | plots - prd |
Output Conf. | xyz - eqa | xyz - eqb | xyz - eqc | xyz - pra | xyz - prb | xyz - prc | xyz - prd |
Please e-mail questions and comments to: Jeff Errington