Chemical Properties of Thiophene, tetrahydro-, 1,1-dioxide (CAS 126-33-0)

Thiophene, tetrahydro-, 1,1-dioxide

PDF Excel Molecule Calculator
InChI
InChI=1S/C4H8O2S/c5-7(6)3-1-2-4-7/h1-4H2
InChI Key
HXJUTPCZVOIRIF-UHFFFAOYSA-N
Formula
C4H8O2S
SMILES
O=S1(=O)CCCC1
Molecular Weight1
120.17
CAS
126-33-0
Other Names
  • 1,1-Dioxide tetrahydrothiofuran
  • 1,1-Dioxidetetrahydrothiophene
  • 1,1-Dioxothiolan
  • 2,3,4,5-Tetrahydrothiophene-1,1-dioxide
  • BONDELANE A
  • Bondolane A
  • CYCLIC TETRAMETHYLENE SULFONE
  • Cyclotetramethylene sulfone
  • Dihydrobutadiene sulfone
  • Dihydrobutadiene sulphone
  • Dioxothiolan
  • NSC 46443
  • Sulfalone
  • Sulfolan
  • Sulfolane
  • Sulpholane
  • Sulphoxaline
  • TETRAHYDROTHIOPHENE DIOXIDE
  • Tetrahydothiophene-1,1-dioxide
  • Tetrahydrothiofen-1,1-dioxid
  • Tetrahydrothiophene 1,1-dioxide
  • Tetramethylene sulfone
  • Thiacyclopentane dioxide
  • Thiocyclopentane-1,1-dioxide
  • Thiolane-1,1-dioxide
  • Thiophan sulfone
  • Thiophane 1,1-dioxide
  • Thiophane dioxide
  • Thiophene, 1,1-dioxide-tetrahydro-
  • thiolane 1,1-dioxide
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Physical Properties

Property Value Unit Source
Δf -434.74 kJ/mol Joback Calculated Property
Δfgas -495.03 kJ/mol Joback Calculated Property
Δfus 9.88 kJ/mol Joback Calculated Property
Δvap 42.69 kJ/mol Joback Calculated Property
log10WS -0.23 Crippen Calculated Property
logPoct/wat 0.195 Crippen Calculated Property
McVol 84.450 ml/mol McGowan Calculated Property
NFPA Fire 1 KDB
NFPA Health 2 KDB
Pc 6328.92 kPa Joback Calculated Property
Tboil 560.48 K Isobari...
Tc 521.90 K Joback Calculated Property
Tfus 237.59 K Joback Calculated Property
Vc 0.320 m3/kmol Joback Calculated Property

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,gas [130.22; 189.37] J/mol×K [337.70; 521.90] Show Hide
Cp,gas 130.22 J/mol×K 337.70 Joback Calculated Property
Cp,gas 141.38 J/mol×K 368.40 Joback Calculated Property
Cp,gas 151.99 J/mol×K 399.10 Joback Calculated Property
Cp,gas 162.09 J/mol×K 429.80 Joback Calculated Property
Cp,gas 171.68 J/mol×K 460.50 Joback Calculated Property
Cp,gas 180.77 J/mol×K 491.20 Joback Calculated Property
Cp,gas 189.37 J/mol×K 521.90 Joback Calculated Property
Cp,liquid [179.50; 213.66] J/mol×K [303.15; 372.20] Show Hide
Cp,liquid 181.50 J/mol×K 303.15 Heat Ca...
Cp,liquid 182.00 J/mol×K 303.15 Molar H...
Cp,liquid 179.90 J/mol×K 304.04 Recomme...
Cp,liquid 179.50 J/mol×K 304.04 Recomme...
Cp,liquid 184.00 J/mol×K 308.15 Molar H...
Cp,liquid 182.42 J/mol×K 308.20 Thermal...
Cp,liquid 181.30 J/mol×K 309.14 Recomme...
Cp,liquid 181.60 J/mol×K 309.15 Recomme...
Cp,liquid 183.50 J/mol×K 312.20 Thermal...
Cp,liquid 185.10 J/mol×K 313.15 Heat Ca...
Cp,liquid 185.00 J/mol×K 313.15 Molar H...
Cp,liquid 182.60 J/mol×K 314.25 Recomme...
Cp,liquid 183.80 J/mol×K 314.25 Recomme...
Cp,liquid 184.70 J/mol×K 316.20 Thermal...
Cp,liquid 186.00 J/mol×K 318.15 Molar H...
Cp,liquid 184.50 J/mol×K 319.35 Recomme...
Cp,liquid 184.70 J/mol×K 319.35 Recomme...
Cp,liquid 185.90 J/mol×K 320.20 Thermal...
Cp,liquid 188.70 J/mol×K 323.15 Heat Ca...
Cp,liquid 188.00 J/mol×K 323.15 Molar H...
Cp,liquid 187.11 J/mol×K 324.20 Thermal...
Cp,liquid 184.40 J/mol×K 324.46 Recomme...
Cp,liquid 185.30 J/mol×K 324.46 Recomme...
Cp,liquid 189.00 J/mol×K 328.15 Molar H...
Cp,liquid 188.79 J/mol×K 328.20 Thermal...
Cp,liquid 187.40 J/mol×K 329.56 Recomme...
Cp,liquid 186.60 J/mol×K 329.56 Recomme...
Cp,liquid 190.47 J/mol×K 332.20 Thermal...
Cp,liquid 191.00 J/mol×K 333.15 Molar H...
Cp,liquid 192.30 J/mol×K 333.15 Heat Ca...
Cp,liquid 188.70 J/mol×K 334.66 Recomme...
Cp,liquid 187.90 J/mol×K 334.67 Recomme...
Cp,liquid 192.39 J/mol×K 336.20 Thermal...
Cp,liquid 193.00 J/mol×K 338.15 Molar H...
Cp,liquid 188.50 J/mol×K 339.77 Recomme...
Cp,liquid 189.70 J/mol×K 339.77 Recomme...
Cp,liquid 194.32 J/mol×K 340.20 Thermal...
Cp,liquid 194.30 J/mol×K 343.15 Heat Ca...
Cp,liquid 194.00 J/mol×K 343.15 Molar H...
Cp,liquid 196.36 J/mol×K 344.20 Thermal...
Cp,liquid 190.20 J/mol×K 344.88 Recomme...
Cp,liquid 190.20 J/mol×K 344.88 Recomme...
Cp,liquid 197.00 J/mol×K 348.15 Molar H...
Cp,liquid 198.52 J/mol×K 348.20 Thermal...
Cp,liquid 192.00 J/mol×K 349.98 Recomme...
Cp,liquid 192.50 J/mol×K 349.98 Recomme...
Cp,liquid 200.81 J/mol×K 352.20 Thermal...
Cp,liquid 197.80 J/mol×K 353.15 Heat Ca...
Cp,liquid 199.00 J/mol×K 353.15 Molar H...
Cp,liquid 193.40 J/mol×K 355.09 Recomme...
Cp,liquid 192.30 J/mol×K 355.09 Recomme...
Cp,liquid 203.21 J/mol×K 356.20 Thermal...
Cp,liquid 205.73 J/mol×K 360.20 Thermal...
Cp,liquid 208.26 J/mol×K 364.20 Thermal...
Cp,liquid 210.90 J/mol×K 368.20 Thermal...
Cp,liquid 213.66 J/mol×K 372.20 Thermal...
η [0.0014150; 0.0102280] Pa×s [303.15; 423.15] Show Hide
η 0.0100700 Pa×s 303.15 Densiti...
η 0.0100742 Pa×s 303.15 Excess ...
η 0.0102280 Pa×s 303.15 Viscome...
η 0.0100304 Pa×s 303.15 Densiti...
η 0.0087947 Pa×s 308.15 Densiti...
η 0.0090460 Pa×s 308.15 Viscome...
η 0.0091940 Pa×s 308.20 Phase e...
η 0.0078080 Pa×s 313.15 Densiti...
η 0.0078440 Pa×s 313.15 Viscome...
η 0.0078365 Pa×s 313.15 Densiti...
η 0.0081160 Pa×s 313.20 Phase e...
η 0.0065740 Pa×s 318.15 Viscome...
η 0.0072010 Pa×s 318.20 Phase e...
η 0.0061750 Pa×s 323.15 Viscome...
η 0.0061940 Pa×s 323.15 Densiti...
η 0.0061936 Pa×s 323.15 Excess ...
η 0.0064390 Pa×s 323.20 Phase e...
η 0.0051910 Pa×s 328.15 Viscome...
η 0.0057720 Pa×s 328.20 Phase e...
η 0.0048870 Pa×s 333.15 Viscome...
η 0.0050090 Pa×s 333.15 Densiti...
η 0.0051990 Pa×s 333.20 Phase e...
η 0.0043100 Pa×s 338.15 Viscome...
η 0.0047140 Pa×s 338.20 Phase e...
η 0.0042140 Pa×s 343.15 Viscome...
η 0.0041260 Pa×s 343.15 Densiti...
η 0.0042680 Pa×s 343.20 Phase e...
η 0.0035310 Pa×s 353.15 Viscome...
η 0.0034400 Pa×s 353.15 Densiti...
η 0.0030110 Pa×s 363.15 Viscome...
η 0.0025760 Pa×s 373.15 Viscome...
η 0.0022530 Pa×s 383.15 Viscome...
η 0.0019870 Pa×s 393.15 Viscome...
η 0.0017610 Pa×s 403.15 Viscome...
η 0.0015710 Pa×s 413.15 Viscome...
η 0.0014150 Pa×s 423.15 Viscome...
Pvap [0.01; 4144.00] kPa [333.15; 829.00] Show Hide
Pvap 0.01 kPa 333.15 Vapor l...
Pvap 0.04 kPa 353.15 Vapor l...
Pvap 103.60 kPa 560.20 Critica...
Pvap 203.90 kPa 594.40 Critica...
Pvap 350.20 kPa 626.30 Critica...
Pvap 556.80 kPa 656.30 Critica...
Pvap 829.20 kPa 685.10 Critica...
Pvap 1181.00 kPa 713.20 Critica...
Pvap 1665.00 kPa 742.00 Critica...
Pvap 2363.00 kPa 773.40 Critica...
Pvap 3185.00 kPa 802.70 Critica...
Pvap 4144.00 kPa 829.00 Critica...
n0 [1.48150; 1.48230]   [303.15; 303.15] Show Hide
n0 1.48230 303.15 Phase e...
n0 1.48150 303.15 (Liquid...
ρl [1206.00; 1266.40] kg/m3 [298.15; 363.15] Show Hide
ρl 1266.40 kg/m3 298.15 Experim...
ρl 1265.75 kg/m3 303.15 Measure...
ρl 1262.00 kg/m3 303.15 Measuri...
ρl 1260.10 kg/m3 303.15 Volumet...
ρl 1262.90 kg/m3 303.15 Density...
ρl 1259.40 kg/m3 303.15 Experim...
ρl 1255.70 kg/m3 308.15 Volumet...
ρl 1251.30 kg/m3 313.15 Volumet...
ρl 1253.00 kg/m3 313.15 Measuri...
ρl 1254.10 kg/m3 313.15 Density...
ρl 1251.70 kg/m3 313.15 Experim...
ρl 1244.00 kg/m3 323.15 Measuri...
ρl 1245.20 kg/m3 323.15 Density...
ρl 1244.00 kg/m3 323.15 Experim...
ρl 1235.40 kg/m3 333.15 Experim...
ρl 1236.60 kg/m3 333.15 Density...
ρl 1235.00 kg/m3 333.15 Measuri...
ρl 1225.00 kg/m3 343.15 Experim...
ρl 1226.00 kg/m3 343.15 Measuri...
ρl 1228.10 kg/m3 343.15 Density...
ρl 1215.00 kg/m3 353.15 Experim...
ρl 1218.00 kg/m3 353.15 Measuri...
ρl 1206.00 kg/m3 363.15 Experim...
ρl 1209.00 kg/m3 363.15 Measuri...
csound,fluid [1558.00; 1588.00] m/s [303.15; 313.15] Show Hide
csound,fluid 1588.00 m/s 303.15 Densiti...
csound,fluid 1576.00 m/s 308.15 Densiti...
csound,fluid 1558.00 m/s 313.15 Densiti...
γ [0.05; 0.05] N/m [303.15; 343.15] Show Hide
γ 0.05 N/m 303.15 Densiti...
γ 0.05 N/m 313.15 Densiti...
γ 0.05 N/m 323.15 Densiti...
γ 0.05 N/m 333.15 Densiti...
γ 0.05 N/m 343.15 Densiti...

Correlations

Property Value Unit Temperature (K) Source
Pvap [1.33; 202.66] kPa [416.57; 592.15] The Yaw... Show Hide
Equationln(Pvp) = A + B/(T + C)
Coefficient A1.51896e+01
Coefficient B-5.14444e+03
Coefficient C-7.13560e+01
Temperature range, min.416.57
Temperature range, max.592.15
Pvap 1.33 kPa 416.57 Calculated Property
Pvap 2.96 kPa 436.08 Calculated Property
Pvap 6.05 kPa 455.59 Calculated Property
Pvap 11.56 kPa 475.10 Calculated Property
Pvap 20.80 kPa 494.61 Calculated Property
Pvap 35.54 kPa 514.11 Calculated Property
Pvap 58.03 kPa 533.62 Calculated Property
Pvap 91.06 kPa 553.13 Calculated Property
Pvap 137.98 kPa 572.64 Calculated Property
Pvap 202.66 kPa 592.15 Calculated Property
Pvap [8.05e-04; 5105.08] kPa [300.75; 849.00] KDB Vap... Show Hide
Equationln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A1.04677e+02
Coefficient B-1.21143e+04
Coefficient C-1.26025e+01
Coefficient D4.33097e-06
Temperature range, min.300.75
Temperature range, max.849.00
Pvap 8.05e-04 kPa 300.75 Calculated Property
Pvap 0.08 kPa 361.67 Calculated Property
Pvap 1.79 kPa 422.58 Calculated Property
Pvap 15.45 kPa 483.50 Calculated Property
Pvap 74.95 kPa 544.42 Calculated Property
Pvap 250.31 kPa 605.33 Calculated Property
Pvap 651.69 kPa 666.25 Calculated Property
Pvap 1433.40 kPa 727.17 Calculated Property
Pvap 2811.47 kPa 788.08 Calculated Property
Pvap 5105.08 kPa 849.00 Calculated Property

Similar Compounds

Thiophene, tetrahydro-, 1-oxide. Butane, 1,1'-sulfonylbis-. Butane, 1-(ethylsulfonyl)-. Butane, 1-(methylsulfonyl)-. 2H-Thiopyran, tetrahydro-, 1,1-dioxide. Butane, 1,1'-sulfinylbis-. Octane, 1,1'-sulfonylbis-. Butane, 1-(ethylsulfinyl)-. 2H-Thiopyran, tetrahydro-, 1-oxide. Butane, 1-(methylsulfinyl)-. Propane, 1,1'-sulfonylbis-. Ethyl n-propyl sulfone. Thiophene, tetrahydro-3-methyl-, 1,1-dioxide. Propanesulfonylacetonitrile. Sulforaphane nitrile.

Find more compounds similar to Thiophene, tetrahydro-, 1,1-dioxide.

Mixtures

Find more mixtures with Thiophene, tetrahydro-, 1,1-dioxide.

Sources

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.