Chemical Properties of Methyl formate (CAS 107-31-3)

Methyl formate

InChI
InChI=1S/C2H4O2/c1-4-2-3/h2H,1H3
InChI Key
TZIHFWKZFHZASV-UHFFFAOYSA-N
Formula
C2H4O2
SMILES
COC=O
Molecular Weight1
60.05
CAS
107-31-3
Other Names
  • Formiate de methyle
  • HCOOCH3
  • METHYL ESTER FORMIC ACID
  • Methanoic acid methyl ester
  • Methyl ester of formic acid
  • Methylester kyseliny mravenci
  • Methylformiaat
  • Methylformiat
  • Mravencan methylnaty
  • UN 1243
  • formic acid, methyl ester
  • methanoic acid, methyl ester
  • methyl methanoate
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Physical Properties

Property Value Unit Source
ω [0.2520; 0.2570]   Show Hide
ω 0.2520 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.2530 ChemSep v8.3 pure component data Compiled value
ω 0.2570 KDB
PAff 782.50 kJ/mol NIST
Tig 729.26 K KDB
BasG 751.50 kJ/mol NIST
ΔcH°liquid -972.61 ± 0.59 kJ/mol NIST
μ [1.77; 1.80] debye Show Hide
μ 1.77 debye ChemSep v8.3 pure component data Compiled value
μ 1.80 debye KDB
η 0.0003000 Pa×s Densities and Viscosities of 1-Butyl-3-methylimidazolium Tetrafluoroborate + Molecular Solvent Binary Mixtures
LFL 5.00 % in Air KDB
UFL 22.70 % in Air KDB
Tflash,oc 240.93 K KDB
ΔfG° [-297.40; -295.00] kJ/mol Show Hide
ΔfG° -295.00 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfG° -297.40 kJ/mol KDB
ΔfH°gas [-362.00; -336.90] kJ/mol Show Hide
ΔfH°gas -357.80 ± 0.59 kJ/mol Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas -352.40 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -350.00 kJ/mol KDB
ΔfH°gas Outlier -336.90 kJ/mol NIST
ΔfH°gas -349.00 kJ/mol NIST
ΔfH°gas -362.00 kJ/mol NIST
ΔfH°gas -355.50 kJ/mol NIST
ΔfH°liquid [-391.00; -365.90] kJ/mol Show Hide
ΔfH°liquid -365.90 kJ/mol NIST
ΔfH°liquid -378.00 kJ/mol NIST
ΔfH°liquid -391.00 kJ/mol NIST
ΔfH°liquid -386.10 kJ/mol NIST
ΔfusH° 6.99 kJ/mol Joback Calculated Property
ΔvapH° [28.20; 30.60] kJ/mol Show Hide
ΔvapH° 28.60 kJ/mol NIST
ΔvapH° 28.40 kJ/mol NIST
ΔvapH° 29.00 kJ/mol NIST
ΔvapH° 30.60 kJ/mol NIST
ΔvapH° 30.60 kJ/mol NIST
ΔvapH° 28.20 ± 0.04 kJ/mol NIST
IE [10.30; 11.00] eV Show Hide
IE 10.84 eV NIST
IE 10.84 eV NIST
IE 10.70 eV NIST
IE 10.99 eV NIST
IE 10.85 ± 0.05 eV NIST
IE 10.85 eV NIST
IE 10.81 ± 0.01 eV NIST
IE 11.00 eV NIST
IE 10.85 eV NIST
IE Outlier 10.30 eV NIST
log10WS [0.58; 0.58]   Show Hide
log10WS 0.58 Aq. Solubility Prediction
log10WS 0.58 Estimated Solubility
logPoct/wat -0.211 Crippen Calculated Property
McVol 46.480 ml/mol McGowan Calculated Property
NFPA Fire 4 KDB
NFPA Health 2 KDB
NFPA Safety 1 KDB
Pc [5998.00; 6247.00] kPa Show Hide
Pc 6000.00 kPa IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc 5998.44 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 6000.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 5998.00 kPa KDB
Pc 6004.00 ± 60.79 kPa NIST
Pc 6007.50 ± 40.00 kPa NIST
Pc Outlier 6247.00 ± 202.65 kPa NIST
Ptriple 6.88e-03 kPa ChemSep v8.3 pure component data Compiled value
ρc [349.38; 349.38] kg/m3 Show Hide
ρc 349.38 ± 4.80 kg/m3 NIST
ρc 349.38 ± 4.20 kg/m3 NIST
Inp [362.00; 407.00]   Show Hide
Inp 376.00 NIST
Inp 377.00 NIST
Inp 369.00 NIST
Inp 369.00 NIST
Inp 373.00 NIST
Inp 370.00 NIST
Inp 386.00 NIST
Inp 373.00 NIST
Inp 380.00 NIST
Inp 362.00 NIST
Inp 370.00 NIST
Inp 386.00 NIST
Inp 401.10 NIST
Inp 386.00 NIST
Inp 386.00 NIST
Inp 407.00 NIST
Inp 407.00 NIST
Inp 401.10 NIST
Ip [757.00; 779.00]   Show Hide
Ip 779.00 NIST
Ip 757.00 NIST
Ip 779.00 NIST
Ip 761.00 NIST
Ip 779.00 NIST
Tboil [304.65; 307.20] K Show Hide
Tboil 304.70 K Solutions of alkyl methanoates and alkanes: Simultaneous modeling of phase equilibria and mixing properties. Estimation of behavior by UNIFAC with recalculation of parameters
Tboil 304.79 K Isobaric Vapor-Liquid Equilibria and Excess Properties for the Binary Systems of Methyl Esters + Heptane
Tboil 304.70 K Isobaric Vapor-Liquid Equilibrium Data and Excess Properties of Binary Systems Comprised of Alkyl Methanoates + Hexane
Tboil 304.89 K Isobaric Vapor-Liquid Equilibium for the Binary Systems of Methyl Formate with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 101.33 kPa
Tboil 304.90 K ChemSep v8.3 pure component data Compiled value
Tboil 304.80 K KDB
Tboil Outlier 307.20 K NIST
Tboil 304.70 K NIST
Tboil 304.70 K NIST
Tboil 304.65 ± 0.20 K NIST
Tboil 304.82 ± 2.00 K NIST
Tboil 305.05 ± 2.00 K NIST
Tboil 304.65 ± 2.00 K NIST
Tboil 304.90 ± 0.50 K NIST
Tboil 305.15 ± 2.00 K NIST
Tboil 304.65 ± 2.00 K NIST
Tboil 305.00 ± 0.30 K NIST
Tboil 304.85 ± 2.00 K NIST
Tboil 304.90 ± 0.30 K NIST
Tboil 304.90 ± 0.30 K NIST
Tboil 305.05 ± 2.00 K NIST
Tboil 305.65 ± 2.00 K NIST
Tboil 304.95 ± 1.00 K NIST
Tboil 305.40 ± 2.00 K NIST
Tboil Outlier 306.55 ± 2.00 K NIST
Tboil Outlier 306.55 ± 2.00 K NIST
Tc [485.20; 523.70] K Show Hide
Tc 487.20 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc 487.20 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 487.20 K ChemSep v8.3 pure component data Compiled value
Tc 487.20 K KDB
Tc 487.20 K NIST
Tc 487.20 ± 1.00 K NIST
Tc 487.20 ± 1.00 K NIST
Tc Outlier 523.70 ± 20.00 K NIST
Tc 485.20 ± 2.00 K NIST
Tfus [173.15; 174.15] K Show Hide
Tfus 173.15 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 174.15 K ChemSep v8.3 pure component data Compiled value
Tfus 174.00 K KDB
Tfus 173.40 K Aq. Solubility Prediction
Tfus 173.20 ± 2.00 K NIST
Tfus 173.40 ± 0.30 K NIST
Ttriple 174.15 K ChemSep v8.3 pure component data Compiled value
UQi 2.04 ChemSep v8.3 pure component data Compiled value
URi 2.14 ChemSep v8.3 pure component data Compiled value
Vc [0.172; 0.172] m3/kmol Show Hide
Vc 0.172 m3/kmol IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Vc 0.172 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.172 m3/kmol ChemSep v8.3 pure component data Compiled value
Vc 0.172 m3/kmol KDB
Zc [0.2546780; 0.2550000]   Show Hide
Zc 0.2550000 IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Zc 0.2550000 ChemSep v8.3 pure component data Compiled value
Zc 0.2546780 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid [95.50; 130.00] J/mol×K [288.00; 298.75] Show Hide
Cp,liquid 121.30 J/mol×K 288.00 NIST
Cp,liquid 95.50 J/mol×K 297.00 NIST
Cp,liquid 130.00 J/mol×K 298.00 NIST
Cp,liquid 119.70 J/mol×K 298.15 NIST
Cp,liquid 120.57 J/mol×K 298.75 NIST
ΔvapH [27.40; 30.10] kJ/mol [283.00; 374.00] Show Hide
ΔvapH 30.10 kJ/mol 283.00 NIST
ΔvapH 29.60 kJ/mol 292.00 NIST
ΔvapH 28.70 ± 0.10 kJ/mol 293.00 NIST
ΔvapH 27.92 kJ/mol 304.70 NIST
ΔvapH 27.90 ± 0.10 kJ/mol 305.00 NIST
ΔvapH 28.20 kJ/mol 305.10 KDB
ΔvapH 27.40 ± 0.10 kJ/mol 313.00 NIST
ΔvapH 28.40 kJ/mol 374.00 NIST
Pvap [101.32; 114.88] kPa [304.70; 308.15] Show Hide
Pvap 101.32 kPa 304.70 Isobaric Vapor-Liquid Equilibrium Data and Excess Properties of Binary Systems Comprised of Alkyl Methanoates + Hexane
Pvap 114.88 kPa 308.15 Total Vapor Pressure Measurements for 2-Ethoxyethanol with Methyl Acetate, Ethyl Acetate, Propyl Acetate, and Ethyl Propionate at 313.15 K and for 2-Ethoxyethanol with Methyl Formate at 308.15 K
n0 [1.33930; 1.34359]   [293.10; 303.15] Show Hide
n0 1.34359 293.10 Vapor-Liquid Equilibrium for Methoxymethane + Methyl Formate, Methoxymethane + Hexane, and Methyl Formate + Methanol
n0 1.34150 298.15 Thermodynamic study of (alkyl esters + alpha,omega-alkyl dihalides) IV: Hex and Vex for 25 binary mixtures {xC(u-1)H(2u-1)CO2CH3 + (1-x)alpha,omega-BrCH2(CH2)(v-2)CH2Br}, where u = 1 to 5, alpha = 1 and v = omega = 2 to 6
n0 1.34110 298.15 Mixing thermodynamic properties of ester-containing solutions: A study on the ternary (methyl alkanoate (pentanoate and methanoate) + methanol) and the corresponding binaries. New contributions to the (ester + ester) interactions
n0 1.34020 299.15 Excess Properties and Isobaric Vapor-Liquid Equilibria for Binary Mixtures of Methyl Esters + tert-Butanol
n0 1.33930 303.15 Excess Volumes of Binary Solutions of Methyl Formate, Ethyl Formate, Propyl Formate, and Benzyl Acetate with Bromo-, Chloro-, and Nitrobenzenes at (303.15, 308.15, and 313.15) K
ρl [960.85; 980.82] kg/m3 [288.15; 298.15] Show Hide
ρl 980.82 kg/m3 288.15 Isobaric vapor-liquid equilibria for binary mixtures from methyl methanoate, dimethoxymethane and dimethyl carbonate at 101.33 kPa
ρl 977.21 kg/m3 291.15 Experimentation and thermodynamic representations of binaries containing compounds of low boiling points: Pentane and alkylmethanoates
ρl 974.00 kg/m3 293.00 KDB
ρl 966.54 kg/m3 298.15 Experimentation and thermodynamic representations of binaries containing compounds of low boiling points: Pentane and alkylmethanoates
ρl 960.85 kg/m3 298.15 Densities and interfacial tensions for fatty acid methyl esters (from methyl formate to methyl heptanoate) + water demixed mixtures at atmospheric pressure conditions

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [58.45; 151.13] J/mol×K [250.00; 1500.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,gas in J/mol×K, T in K
Coefficient A4.13190e+01
Coefficient B-5.70150e+02
Coefficient C5.13024e+00
Coefficient D-3.42160e-05
Coefficient E-2.71090e-11
Temperature range, min.250.00
Temperature range, max.1500.00
Cp,gas 58.45 J/mol×K 250.00 Calculated Property
Cp,gas 79.83 J/mol×K 388.89 Calculated Property
Cp,gas 97.69 J/mol×K 527.78 Calculated Property
Cp,gas 111.58 J/mol×K 666.67 Calculated Property
Cp,gas 122.35 J/mol×K 805.56 Calculated Property
Cp,gas 130.82 J/mol×K 944.44 Calculated Property
Cp,gas 137.56 J/mol×K 1083.33 Calculated Property
Cp,gas 143.01 J/mol×K 1222.22 Calculated Property
Cp,gas 147.46 J/mol×K 1361.11 Calculated Property
Cp,gas 151.13 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [98.76; 121.14] J/mol×K [174.15; 304.90] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,liquid in J/mol×K, T in K
Coefficient A9.70640e+01
Coefficient B3.37740e+03
Coefficient C-4.92808e+01
Coefficient D2.26480e-01
Coefficient E-2.97630e-04
Temperature range, min.174.15
Temperature range, max.304.90
Cp,liquid 98.76 J/mol×K 174.15 Calculated Property
Cp,liquid 99.19 J/mol×K 188.68 Calculated Property
Cp,liquid 99.99 J/mol×K 203.21 Calculated Property
Cp,liquid 101.26 J/mol×K 217.73 Calculated Property
Cp,liquid 103.16 J/mol×K 232.26 Calculated Property
Cp,liquid 105.82 J/mol×K 246.79 Calculated Property
Cp,liquid 109.28 J/mol×K 261.32 Calculated Property
Cp,liquid 113.34 J/mol×K 275.84 Calculated Property
Cp,liquid 117.54 J/mol×K 290.37 Calculated Property
Cp,liquid 121.14 J/mol×K 304.90 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0006099; 0.0002441] Pa×s [250.00; 343.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-9.94900e+00
Coefficient B1.21440e+03
Coefficient C-5.35620e-01
Coefficient D1.03460e-05
Coefficient E2.00000e+00
Temperature range, min.250.00
Temperature range, max.343.00
η 0.0006099 Pa×s 250.00 Calculated Property
η 0.0005198 Pa×s 260.33 Calculated Property
η 0.0004509 Pa×s 270.67 Calculated Property
η 0.0003975 Pa×s 281.00 Calculated Property
η 0.0003556 Pa×s 291.33 Calculated Property
η 0.0003223 Pa×s 301.67 Calculated Property
η 0.0002959 Pa×s 312.00 Calculated Property
η 0.0002746 Pa×s 322.33 Calculated Property
η 0.0002576 Pa×s 332.67 Calculated Property
η 0.0002441 Pa×s 343.00 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [34.91; 0.62] kJ/mol [174.15; 487.15] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc
Y is ΔvapH in kJ/mol, T in K
Coefficient A7.05780e+01
Coefficient B3.78550e+00
Coefficient C-9.08740e+00
Coefficient D9.60430e+00
Coefficient E-3.78680e+00
Critical temperature, Tc (K)4.87200e+02
Temperature range, min.174.15
Temperature range, max.487.15
ΔvapH 34.91 kJ/mol 174.15 Calculated Property
ΔvapH 33.02 kJ/mol 208.93 Calculated Property
ΔvapH 31.37 kJ/mol 243.71 Calculated Property
ΔvapH 29.68 kJ/mol 278.48 Calculated Property
ΔvapH 27.74 kJ/mol 313.26 Calculated Property
ΔvapH 25.43 kJ/mol 348.04 Calculated Property
ΔvapH 22.65 kJ/mol 382.82 Calculated Property
ΔvapH 19.24 kJ/mol 417.59 Calculated Property
ΔvapH 14.63 kJ/mol 452.37 Calculated Property
ΔvapH 0.62 kJ/mol 487.15 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 4511.72] kPa [224.24; 487.20] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.42260e+01
Coefficient B-2.62106e+03
Coefficient C-3.61910e+01
Temperature range, min.224.24
Temperature range, max.487.20
Pvap 1.33 kPa 224.24 Calculated Property
Pvap 8.69 kPa 253.46 Calculated Property
Pvap 36.31 kPa 282.68 Calculated Property
Pvap 112.07 kPa 311.89 Calculated Property
Pvap 278.69 kPa 341.11 Calculated Property
Pvap 590.95 kPa 370.33 Calculated Property
Pvap 1110.43 kPa 399.55 Calculated Property
Pvap 1899.55 kPa 428.76 Calculated Property
Pvap 3016.54 kPa 457.98 Calculated Property
Pvap 4511.72 kPa 487.20 Calculated Property
Pvap [7.11e-03; 5806.27] kPa [174.15; 487.20] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is Pvap in kPa, T in K
Coefficient A6.37380e+01
Coefficient B-5.40175e+03
Coefficient C-7.33479e+00
Coefficient D5.93434e-06
Coefficient E2.00000e+00
Temperature range, min.174.15
Temperature range, max.487.20
Pvap 7.11e-03 kPa 174.15 Calculated Property
Pvap 0.35 kPa 208.93 Calculated Property
Pvap 5.03 kPa 243.72 Calculated Property
Pvap 33.51 kPa 278.50 Calculated Property
Pvap 137.59 kPa 313.28 Calculated Property
Pvap 408.15 kPa 348.07 Calculated Property
Pvap 966.67 kPa 382.85 Calculated Property
Pvap 1951.53 kPa 417.63 Calculated Property
Pvap 3510.82 kPa 452.42 Calculated Property
Pvap 5806.27 kPa 487.20 Calculated Property
Pvap [7.18e-03; 5921.32] kPa [174.15; 487.20] KDB Vapor Pressure Data Show Hide
Equationln(Y) = A + B/T + C·ln(T) + D·T² + E/T²
Y is Pvap in kPa, T in K
Coefficient A6.57116e+01
Coefficient B-5.45175e+03
Coefficient C-7.66441e+00
Coefficient D6.72918e-06
Coefficient E0.00000e+00
Temperature range, min.174.15
Temperature range, max.487.20
Pvap 7.18e-03 kPa 174.15 Calculated Property
Pvap 0.36 kPa 208.93 Calculated Property
Pvap 5.04 kPa 243.72 Calculated Property
Pvap 33.51 kPa 278.50 Calculated Property
Pvap 137.25 kPa 313.28 Calculated Property
Pvap 406.95 kPa 348.07 Calculated Property
Pvap 965.64 kPa 382.85 Calculated Property
Pvap 1957.94 kPa 417.63 Calculated Property
Pvap 3546.70 kPa 452.42 Calculated Property
Pvap 5921.32 kPa 487.20 Calculated Property
Pvap [67.45; 100.80] kPa [294.00; 304.90] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A5.18305e+00
Coefficient B-1.50221e+01
Coefficient C-2.78540e+02
ReferenceNelson, 1928
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.294.00
Temperature range, max.304.90
Pvap 67.45 kPa 294.00 Calculated Property
Pvap 72.38 kPa 295.21 Calculated Property
Pvap 76.94 kPa 296.42 Calculated Property
Pvap 81.15 kPa 297.63 Calculated Property
Pvap 85.05 kPa 298.84 Calculated Property
Pvap 88.66 kPa 300.06 Calculated Property
Pvap 92.03 kPa 301.27 Calculated Property
Pvap 95.15 kPa 302.48 Calculated Property
Pvap 98.07 kPa 303.69 Calculated Property
Pvap 100.80 kPa 304.90 Calculated Property
Property Value Unit Temperature (K) Source
ρl [1125.12; 358.46] kg/m3 [174.15; 487.15] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A / B^(1 + (1 − T/C)^D)
Y is ρl in kg/m3, T in K
Coefficient A7.28430e+01
Coefficient B2.36190e-01
Coefficient C4.87200e+02
Coefficient D2.46210e-01
Temperature range, min.174.15
Temperature range, max.487.15
ρl 1125.12 kg/m3 174.15 Calculated Property
ρl 1084.26 kg/m3 208.93 Calculated Property
ρl 1041.07 kg/m3 243.71 Calculated Property
ρl 994.96 kg/m3 278.48 Calculated Property
ρl 945.11 kg/m3 313.26 Calculated Property
ρl 890.21 kg/m3 348.04 Calculated Property
ρl 827.99 kg/m3 382.82 Calculated Property
ρl 753.87 kg/m3 417.59 Calculated Property
ρl 655.32 kg/m3 452.37 Calculated Property
ρl 358.46 kg/m3 487.15 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.04; 0.02] N/m [174.15; 304.85] Jasper (1972), surface tension of pure liquid compounds Compiled value Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is γ in N/m, T in K
Coefficient A7.12292e-02
Coefficient B-1.57200e-04
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.174.15
Temperature range, max.304.85
γ 0.04 N/m 174.15 Calculated Property
γ 0.04 N/m 188.67 Calculated Property
γ 0.04 N/m 203.19 Calculated Property
γ 0.04 N/m 217.72 Calculated Property
γ 0.03 N/m 232.24 Calculated Property
γ 0.03 N/m 246.76 Calculated Property
γ 0.03 N/m 261.28 Calculated Property
γ 0.03 N/m 275.81 Calculated Property
γ 0.03 N/m 290.33 Calculated Property
γ 0.02 N/m 304.85 Calculated Property
γ [0.05; 9.60e-04] N/m [174.15; 470.72] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is γ in N/m, T in K
Coefficient A-1.32590e-02
Coefficient B4.71440e+01
Coefficient C-3.04170e+00
Coefficient D1.15900e-03
Coefficient E-8.38170e-06
Temperature range, min.174.15
Temperature range, max.470.72
γ 0.05 N/m 174.15 Calculated Property
γ 0.04 N/m 207.10 Calculated Property
γ 0.03 N/m 240.05 Calculated Property
γ 0.03 N/m 273.01 Calculated Property
γ 0.02 N/m 305.96 Calculated Property
γ 0.02 N/m 338.91 Calculated Property
γ 0.01 N/m 371.86 Calculated Property
γ 0.01 N/m 404.82 Calculated Property
γ 0.00 N/m 437.77 Calculated Property
γ 9.60e-04 N/m 470.72 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.01; 0.13] W/m×K [174.15; 1000.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·T^B / (1 + C/T + D/T²)
Y is λgas in W/m×K, T in K
Coefficient A-8.17050e+05
Coefficient B-2.30160e-01
Coefficient C2.53140e+08
Coefficient D-1.52050e+12
Temperature range, min.174.15
Temperature range, max.1000.00
λgas 0.01 W/m×K 174.15 Calculated Property
λgas 0.01 W/m×K 265.91 Calculated Property
λgas 0.02 W/m×K 357.67 Calculated Property
λgas 0.03 W/m×K 449.43 Calculated Property
λgas 0.04 W/m×K 541.19 Calculated Property
λgas 0.05 W/m×K 632.96 Calculated Property
λgas 0.07 W/m×K 724.72 Calculated Property
λgas 0.09 W/m×K 816.48 Calculated Property
λgas 0.11 W/m×K 908.24 Calculated Property
λgas 0.13 W/m×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.26; 0.14] W/m×K [146.16; 386.16] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is λliquid in W/m×K, T in K
Coefficient A9.03630e-03
Coefficient B2.35940e+01
Coefficient C-1.56270e+00
Coefficient D8.92830e-04
Coefficient E-5.81010e-06
Temperature range, min.146.16
Temperature range, max.386.16
λliquid 0.26 W/m×K 146.16 Calculated Property
λliquid 0.24 W/m×K 172.83 Calculated Property
λliquid 0.23 W/m×K 199.49 Calculated Property
λliquid 0.22 W/m×K 226.16 Calculated Property
λliquid 0.21 W/m×K 252.83 Calculated Property
λliquid 0.19 W/m×K 279.49 Calculated Property
λliquid 0.18 W/m×K 306.16 Calculated Property
λliquid 0.17 W/m×K 332.83 Calculated Property
λliquid 0.15 W/m×K 359.49 Calculated Property
λliquid 0.14 W/m×K 386.16 Calculated Property

Similar Compounds

HCOOCH radical anion. (CD3)2O. Dimethyl ether. Methyl radical, methoxy-. Carbonochloridic acid, methyl ester. Carbonic acid, dimethyl ester. Methoxycarbonylsulfenyl chloride. Methane, chloromethoxy-. 2-Propynoic acid, methyl ester. BROMOMETHYL METHYL ETHER. Acetic acid, oxo-, methyl ester. «alpha»,«alpha»-Dichloromethyl methyl ether. Carbamic acid, methyl ester. Acetic acid, methyl ester. CF3OCH3.

Find more compounds similar to Methyl formate.

Mixtures

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Sources

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