Mixture of Butane + Thiophene, tetrahydro-

Datasets

1. P_vap - Vapor or sublimation pressure, kPa

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	318.35	6.90
0.0000	346.97	22.20
0.0145	346.97	50.40
0.0170	318.35	24.60
0.0333	346.97	85.00
0.0335	318.35	40.80
0.0506	346.97	114.80
0.0569	318.34	62.30
0.0926	346.97	180.80
0.1064	318.34	102.60
0.1399	346.97	245.60
0.1526	318.34	134.80
0.1873	346.97	302.30
0.2012	318.34	164.10
0.2342	346.97	351.60
0.2494	318.34	189.30
0.2830	346.98	397.00
0.2986	318.35	211.80
0.3342	346.97	439.30
0.3476	318.34	231.60
0.3854	346.97	477.20
0.3997	318.35	250.30
0.4363	346.97	511.80
0.4496	318.35	266.50
0.4870	346.96	544.60
0.4870	346.96	544.60
0.4870	346.96	544.60
0.4875	346.97	544.20
0.4997	318.35	281.90
0.4999	318.35	281.60
0.5359	346.97	574.00
0.5492	318.35	295.70
0.5861	346.97	602.90
0.5993	318.34	309.10
0.6362	346.96	631.30
0.6488	318.34	322.30
0.6861	346.96	659.60
0.7005	318.35	336.00
0.7366	346.97	689.20
0.7494	318.35	349.40
0.7886	346.97	720.90
0.7983	318.35	363.50
0.8410	346.97	755.00
0.8506	318.35	379.70
0.8929	346.97	791.80
0.9003	318.35	396.70
0.9476	318.35	414.60
0.9759	318.35	426.50
0.9898	346.97	871.80
0.9948	318.35	434.90
1.0000	318.35	437.50
1.0000	346.97	881.70

Sources

• Vapor-Liquid Equilibrium for Tetrahydrothiophene + n-Butane, + trans-2-Butene, + 2-Methylpropane, and + 2-Methylpropene

Note: These property values are available through the Cheméo API. A free account gives you an access key.