Chemical Properties of Ethane, 1,1-dichloro- (CAS 75-34-3)

InChI

InChI=1S/C2H4Cl2/c1-2(3)4/h2H,1H3

InChI Key

SCYULBFZEHDVBN-UHFFFAOYSA-N

Formula

C2H4Cl2

SMILES

CC(Cl)Cl

Molecular Weight¹

98.96

CAS

75-34-3

Other Names

• 1,1-Dichloorethaan
• 1,1-Dichloraethan
• 1,1-Dichlorethane
• 1,1-Dichloroethane [R 150a]
• 1,1-Dicloroetano
• 1,1-dichloroethane
• Aethylidenchlorid
• Assymmetrical Dichloroethane
• CH3CHCl2
• Chlorure d'ethylidene
• Cloruro di etilidene
• Dichloromethylmethane
• Ethylidene dichloride
• NCI-C04535
• R-150a
• REFRIGERANT-150A
• Rcra waste number U076
• UN 2362
• ethylidene chloride
• freon 150a

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• γ : Surface Tension (N/m).
• Δ_vapS : Entropy of vaporization at a given temperature (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.2400; 0.2480]
ω	0.2480		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2440		ChemSep v8.3 pure component data Compiled value
ω	0.2400		KDB
ΔcH°liquid	-1246.80 ± 8.40	kJ/mol	NIST
μ	[2.00; 2.06]	debye
μ	2.06	debye	ChemSep v8.3 pure component data Compiled value
μ	2.00	debye	KDB
ΔfG°	[-73.14; -72.59]	kJ/mol
ΔfG°	-72.59	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-73.14	kJ/mol	KDB
ΔfH°gas	[-132.50; -127.40]	kJ/mol
ΔfH°gas	-127.40 ± 1.10	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	-129.41	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-130.00	kJ/mol	KDB
ΔfH°gas	-132.50 ± 3.50	kJ/mol	NIST
ΔfH°gas	-127.60 ± 1.10	kJ/mol	NIST
ΔfH°liquid	-163.30 ± 3.50	kJ/mol	NIST
ΔfusH°	5.81	kJ/mol	Joback Calculated Property
ΔvapH°	[30.60; 30.83]	kJ/mol
ΔvapH°	30.77	kJ/mol	NIST
ΔvapH°	30.83 ± 0.08	kJ/mol	NIST
ΔvapH°	30.62 ± 0.14	kJ/mol	NIST
ΔvapH°	30.60 ± 0.10	kJ/mol	NIST
IE	[11.02; 11.23]	eV
IE	11.04 ± 0.02	eV	NIST
IE	11.02	eV	NIST
IE	11.06	eV	NIST
IE	11.23 ± 0.02	eV	NIST
log10WS	[-1.29; -1.29]
log10WS	-1.29		Aq. Solubility Prediction
log10WS	-1.29		Estimated Solubility
logPoct/wat	1.810		Crippen Calculated Property
McVol	63.520	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
Pc	[5060.00; 5100.00]	kPa
Pc	5060.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Pc	5066.25	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	5100.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	5070.00	kPa	KDB
Pc	5061.00 ± 10.00	kPa	NIST
Ptriple	2.21e-03	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[541.00; 601.60]
Inp	592.20		NIST
Inp	593.30		NIST
Inp	601.60		NIST
Inp	598.90		NIST
Inp	594.20		NIST
Inp	590.60		NIST
Inp	585.90		NIST
Inp	560.00		NIST
Inp	564.00		NIST
Inp	568.00		NIST
Inp	570.00		NIST
Inp	566.00		NIST
Inp	553.00		NIST
Inp	600.00		NIST
Inp	541.00		NIST
Inp	568.00		NIST
Inp	568.00		NIST
Inp	559.00		NIST
Inp	579.00		NIST
Inp	559.00		NIST
Inp	563.00		NIST
Inp	563.00		NIST
Inp	553.00		NIST
Inp	568.00		NIST
Inp	563.00		NIST
Ip	[881.00; 901.48]
Ip	901.00		NIST
Ip	900.52		NIST
Ip	901.48		NIST
Ip	886.92		NIST
Ip	881.00		NIST
Ip	901.00		NIST
S°liquid	211.75	J/mol×K	NIST
Tboil	[273.15; 331.15]	K
Tboil	330.45	K	ChemSep v8.3 pure component data Compiled value
Tboil	330.50	K	KDB
Tboil	330.50	K	NIST
Tboil	330.44 ± 0.20	K	NIST
Tboil	330.44 ± 0.20	K	NIST
Tboil	330.44 ± 0.20	K	NIST
Tboil	330.25 ± 0.20	K	NIST
Tboil	330.40	K	NIST
Tboil	330.50 ± 0.50	K	NIST
Tboil	330.45 ± 0.30	K	NIST
Tboil	330.55 ± 0.20	K	NIST
Tboil	330.60 ± 0.50	K	NIST
Tboil	330.40 ± 0.50	K	NIST
Tboil	331.00 ± 7.00	K	NIST
Tboil	330.46 ± 0.20	K	NIST
Tboil	330.20 ± 0.20	K	NIST
Tboil	330.40 ± 0.50	K	NIST
Tboil	Outlier 273.15 ± 0.50	K	NIST
Tboil	330.50 ± 0.30	K	NIST
Tboil	331.15 ± 2.00	K	NIST
Tboil	330.00 ± 2.00	K	NIST
Tc	[523.00; 523.40]	K
Tc	523.40	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Tc	523.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	523.00	K	ChemSep v8.3 pure component data Compiled value
Tc	523.00	K	KDB
Tc	523.40 ± 0.20	K	NIST
Tfus	[174.00; 176.70]	K
Tfus	176.20	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	176.19	K	ChemSep v8.3 pure component data Compiled value
Tfus	176.19	K	KDB
Tfus	176.20	K	Aq. Solubility Prediction
Tfus	Outlier 174.00 ± 1.50	K	NIST
Tfus	176.70 ± 1.00	K	NIST
Tfus	176.50 ± 0.30	K	NIST
Ttriple	[176.18; 176.19]	K
Ttriple	176.19	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	176.19	K	ChemSep v8.3 pure component data Compiled value
Ttriple	176.18 ± 0.02	K	NIST
UQi	2.53		ChemSep v8.3 pure component data Compiled value
URi	2.96		ChemSep v8.3 pure component data Compiled value
Vc	[0.236; 0.240]	m3/kmol
Vc	0.236	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Vc	0.240	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.236	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.236	m3/kmol	KDB
Zc	[0.2740000; 0.2770000]
Zc	0.2740000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Zc	0.2770000		ChemSep v8.3 pure component data Compiled value
Zc	0.2751580		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[119.60; 127.20]	J/mol×K	[180.00; 300.00]
Cp,liquid	119.60	J/mol×K	180.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	119.90	J/mol×K	190.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	120.20	J/mol×K	200.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	120.60	J/mol×K	210.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	121.10	J/mol×K	220.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	121.60	J/mol×K	230.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	122.10	J/mol×K	240.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	122.70	J/mol×K	250.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	123.40	J/mol×K	260.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	124.10	J/mol×K	270.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	124.30	J/mol×K	273.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	124.80	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	125.60	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	127.20	J/mol×K	298.00	NIST
Cp,liquid	120.90	J/mol×K	298.00	NIST
Cp,liquid	126.40	J/mol×K	298.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	126.27	J/mol×K	298.15	NIST
Cp,liquid	126.50	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
ΔfusH	[7.87; 7.87]	kJ/mol	[176.18; 176.20]
ΔfusH	7.87	kJ/mol	176.18	NIST
ΔfusH	7.87	kJ/mol	176.20	NIST
ΔfusH	7.87	kJ/mol	176.20	NIST
ΔvapH	[28.20; 34.40]	kJ/mol	[262.00; 449.00]
ΔvapH	31.90	kJ/mol	262.00	NIST
ΔvapH	34.40	kJ/mol	271.50	NIST
ΔvapH	31.00	kJ/mol	293.00	NIST
ΔvapH	31.00 ± 29.00	kJ/mol	293.00	NIST
ΔvapH	28.85	kJ/mol	330.40	NIST
ΔvapH	28.70	kJ/mol	330.70	KDB
ΔvapH	33.50	kJ/mol	335.50	NIST
ΔvapH	29.20	kJ/mol	429.00	NIST
ΔvapH	28.20	kJ/mol	449.00	NIST
ρl	1168.00	kg/m3	298.00	KDB
ΔfusS	44.67	J/mol×K	176.18	NIST
γ	0.02	N/m	293.20	KDB
ΔvapS	105.81	J/mol×K	293.00	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[52.46; 156.23]	J/mol×K	[150.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			4.56610e+01
Coefficient B			-4.49920e+02
Coefficient C			4.89424e+00
Coefficient D			1.54960e-04
Coefficient E			-5.38290e-08
Temperature range, min.			150.00
Temperature range, max.			1500.00
Cp,gas	52.46	J/mol×K	150.00	Calculated Property
Cp,gas	76.73	J/mol×K	300.00	Calculated Property
Cp,gas	97.77	J/mol×K	450.00	Calculated Property
Cp,gas	113.56	J/mol×K	600.00	Calculated Property
Cp,gas	125.52	J/mol×K	750.00	Calculated Property
Cp,gas	134.80	J/mol×K	900.00	Calculated Property
Cp,gas	142.12	J/mol×K	1050.00	Calculated Property
Cp,gas	147.94	J/mol×K	1200.00	Calculated Property
Cp,gas	152.58	J/mol×K	1350.00	Calculated Property
Cp,gas	156.23	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[119.58; 130.04]	J/mol×K	[176.19; 330.45]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.15470e+02
Coefficient B			4.79340e+02
Coefficient C			-5.70686e+00
Coefficient D			2.95110e-02
Coefficient E			-2.57940e-05
Temperature range, min.			176.19
Temperature range, max.			330.45
Cp,liquid	119.58	J/mol×K	176.19	Calculated Property
Cp,liquid	120.01	J/mol×K	193.33	Calculated Property
Cp,liquid	120.62	J/mol×K	210.47	Calculated Property
Cp,liquid	121.40	J/mol×K	227.61	Calculated Property
Cp,liquid	122.35	J/mol×K	244.75	Calculated Property
Cp,liquid	123.50	J/mol×K	261.89	Calculated Property
Cp,liquid	124.84	J/mol×K	279.03	Calculated Property
Cp,liquid	126.38	J/mol×K	296.17	Calculated Property
Cp,liquid	128.11	J/mol×K	313.31	Calculated Property
Cp,liquid	130.04	J/mol×K	330.45	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0040774; 0.0001775]	Pa×s	[176.19; 423.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-9.78030e+00
Coefficient B			8.91160e+02
Coefficient C			-1.48660e-01
Coefficient D			-3.58840e-07
Coefficient E			2.00000e+00
Temperature range, min.			176.19
Temperature range, max.			423.00
η	0.0040774	Pa×s	176.19	Calculated Property
η	0.0020117	Pa×s	203.61	Calculated Property
η	0.0011693	Pa×s	231.04	Calculated Property
η	0.0007601	Pa×s	258.46	Calculated Property
η	0.0005350	Pa×s	285.88	Calculated Property
η	0.0003994	Pa×s	313.31	Calculated Property
η	0.0003117	Pa×s	340.73	Calculated Property
η	0.0002519	Pa×s	368.15	Calculated Property
η	0.0002091	Pa×s	395.58	Calculated Property
η	0.0001775	Pa×s	423.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[36.27; 11.06]	kJ/mol	[176.19; 504.75]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			4.45877e+01
Coefficient B			5.55838e-01
Coefficient C			2.09485e-02
Coefficient D			-7.22234e-01
Coefficient E			5.69630e-01
Critical temperature, Tc (K)			5.23000e+02
Temperature range, min.			176.19
Temperature range, max.			504.75
ΔvapH	36.27	kJ/mol	176.19	Calculated Property
ΔvapH	34.65	kJ/mol	212.70	Calculated Property
ΔvapH	33.03	kJ/mol	249.20	Calculated Property
ΔvapH	31.38	kJ/mol	285.71	Calculated Property
ΔvapH	29.60	kJ/mol	322.22	Calculated Property
ΔvapH	27.60	kJ/mol	358.72	Calculated Property
ΔvapH	25.19	kJ/mol	395.23	Calculated Property
ΔvapH	22.12	kJ/mol	431.74	Calculated Property
ΔvapH	17.90	kJ/mol	468.24	Calculated Property
ΔvapH	11.06	kJ/mol	504.75	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 5049.80]	kPa	[240.70; 523.00]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.45193e+01
Coefficient B			-2.92184e+03
Coefficient C			-3.53950e+01
Temperature range, min.			240.70
Temperature range, max.			523.00
Pvap	1.33	kPa	240.70	Calculated Property
Pvap	8.79	kPa	272.07	Calculated Property
Pvap	37.28	kPa	303.43	Calculated Property
Pvap	116.81	kPa	334.80	Calculated Property
Pvap	294.69	kPa	366.17	Calculated Property
Pvap	633.36	kPa	397.53	Calculated Property
Pvap	1204.92	kPa	428.90	Calculated Property
Pvap	2084.61	kPa	460.27	Calculated Property
Pvap	3344.71	kPa	491.63	Calculated Property
Pvap	5049.80	kPa	523.00	Calculated Property
Pvap	[2.21e-03; 5087.65]	kPa	[176.19; 523.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			5.96263e+01
Coefficient B			-5.49241e+03
Coefficient C			-6.71599e+00
Coefficient D			5.29878e-06
Coefficient E			2.00000e+00
Temperature range, min.			176.19
Temperature range, max.			523.00
Pvap	2.21e-03	kPa	176.19	Calculated Property
Pvap	0.17	kPa	214.72	Calculated Property
Pvap	3.03	kPa	253.26	Calculated Property
Pvap	22.97	kPa	291.79	Calculated Property
Pvap	101.89	kPa	330.33	Calculated Property
Pvap	318.20	kPa	368.86	Calculated Property
Pvap	782.33	kPa	407.40	Calculated Property
Pvap	1627.09	kPa	445.93	Calculated Property
Pvap	3003.58	kPa	484.47	Calculated Property
Pvap	5087.65	kPa	523.00	Calculated Property
Pvap	[1.98e-03; 5117.20]	kPa	[176.19; 523.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			7.31701e+01
Coefficient B			-5.95760e+03
Coefficient C			-8.86262e+00
Coefficient D			8.18126e-06
Coefficient E			0.00000e+00
Temperature range, min.			176.19
Temperature range, max.			523.00
Pvap	1.98e-03	kPa	176.19	Calculated Property
Pvap	0.17	kPa	214.72	Calculated Property
Pvap	3.07	kPa	253.26	Calculated Property
Pvap	23.22	kPa	291.79	Calculated Property
Pvap	101.84	kPa	330.33	Calculated Property
Pvap	314.21	kPa	368.86	Calculated Property
Pvap	766.52	kPa	407.40	Calculated Property
Pvap	1593.33	kPa	445.93	Calculated Property
Pvap	2966.07	kPa	484.47	Calculated Property
Pvap	5117.20	kPa	523.00	Calculated Property
Pvap	[0.86; 22.01]	kPa	[234.38; 290.76]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42629e+01
Coefficient B			-2.79843e+03
Coefficient C			-4.02600e+01
Reference			Li and Pitzer, 1956
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			234.38
Temperature range, max.			290.76
Pvap	0.86	kPa	234.38	Calculated Property
Pvap	1.35	kPa	240.64	Calculated Property
Pvap	2.06	kPa	246.91	Calculated Property
Pvap	3.06	kPa	253.17	Calculated Property
Pvap	4.46	kPa	259.44	Calculated Property
Pvap	6.36	kPa	265.70	Calculated Property
Pvap	8.89	kPa	271.97	Calculated Property
Pvap	12.22	kPa	278.23	Calculated Property
Pvap	16.53	kPa	284.50	Calculated Property
Pvap	22.01	kPa	290.76	Calculated Property
Pvap	[0.13; 100.78]	kPa	[212.50; 330.60]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43256e+01
Coefficient B			-2.83024e+03
Coefficient C			-3.92040e+01
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			212.50
Temperature range, max.			330.60
Pvap	0.13	kPa	212.50	Calculated Property
Pvap	0.42	kPa	225.62	Calculated Property
Pvap	1.15	kPa	238.74	Calculated Property
Pvap	2.76	kPa	251.87	Calculated Property
Pvap	5.99	kPa	264.99	Calculated Property
Pvap	11.93	kPa	278.11	Calculated Property
Pvap	22.10	kPa	291.23	Calculated Property
Pvap	38.53	kPa	304.36	Calculated Property
Pvap	63.75	kPa	317.48	Calculated Property
Pvap	100.78	kPa	330.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1340.72; 684.20]	kg/m3	[176.19; 504.75]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			1.09419e+02
Coefficient B			2.65360e-01
Coefficient C			5.23000e+02
Coefficient D			2.87030e-01
Temperature range, min.			176.19
Temperature range, max.			504.75
ρl	1340.72	kg/m3	176.19	Calculated Property
ρl	1291.95	kg/m3	212.70	Calculated Property
ρl	1240.92	kg/m3	249.20	Calculated Property
ρl	1187.10	kg/m3	285.71	Calculated Property
ρl	1129.77	kg/m3	322.22	Calculated Property
ρl	1067.79	kg/m3	358.72	Calculated Property
ρl	999.38	kg/m3	395.23	Calculated Property
ρl	921.16	kg/m3	431.74	Calculated Property
ρl	825.51	kg/m3	468.24	Calculated Property
ρl	684.20	kg/m3	504.75	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[176.15; 330.45]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			5.94256e-02
Coefficient B			-1.18600e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			176.15
Temperature range, max.			330.45
γ	0.04	N/m	176.15	Calculated Property
γ	0.04	N/m	193.29	Calculated Property
γ	0.03	N/m	210.44	Calculated Property
γ	0.03	N/m	227.58	Calculated Property
γ	0.03	N/m	244.73	Calculated Property
γ	0.03	N/m	261.87	Calculated Property
γ	0.03	N/m	279.02	Calculated Property
γ	0.02	N/m	296.16	Calculated Property
γ	0.02	N/m	313.31	Calculated Property
γ	0.02	N/m	330.45	Calculated Property
γ	[0.04; 8.05e-04]	N/m	[176.19; 504.75]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-4.32740e-02
Coefficient B			-3.82450e+00
Coefficient C			-2.07090e+00
Coefficient D			-1.97040e-03
Coefficient E			-1.91290e-07
Temperature range, min.			176.19
Temperature range, max.			504.75
γ	0.04	N/m	176.19	Calculated Property
γ	0.04	N/m	212.70	Calculated Property
γ	0.03	N/m	249.20	Calculated Property
γ	0.03	N/m	285.71	Calculated Property
γ	0.02	N/m	322.22	Calculated Property
γ	0.02	N/m	358.72	Calculated Property
γ	0.01	N/m	395.23	Calculated Property
γ	0.01	N/m	431.74	Calculated Property
γ	0.00	N/m	468.24	Calculated Property
γ	8.05e-04	N/m	504.75	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.07]	W/m×K	[176.19; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			1.33810e-04
Coefficient B			1.01000e+00
Coefficient C			1.04250e+03
Coefficient D			-2.44200e+03
Temperature range, min.			176.19
Temperature range, max.			1000.00
λgas	0.00	W/m×K	176.19	Calculated Property
λgas	0.01	W/m×K	267.72	Calculated Property
λgas	0.01	W/m×K	359.26	Calculated Property
λgas	0.02	W/m×K	450.79	Calculated Property
λgas	0.03	W/m×K	542.33	Calculated Property
λgas	0.03	W/m×K	633.86	Calculated Property
λgas	0.04	W/m×K	725.40	Calculated Property
λgas	0.05	W/m×K	816.93	Calculated Property
λgas	0.06	W/m×K	908.47	Calculated Property
λgas	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.08]	W/m×K	[156.90; 416.90]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			1.13570e-02
Coefficient B			-6.40860e+01
Coefficient C			-9.81270e-01
Coefficient D			-3.94690e-03
Coefficient E			6.61060e-07
Temperature range, min.			156.90
Temperature range, max.			416.90
λliquid	0.15	W/m×K	156.90	Calculated Property
λliquid	0.14	W/m×K	185.79	Calculated Property
λliquid	0.13	W/m×K	214.68	Calculated Property
λliquid	0.13	W/m×K	243.57	Calculated Property
λliquid	0.12	W/m×K	272.46	Calculated Property
λliquid	0.11	W/m×K	301.34	Calculated Property
λliquid	0.10	W/m×K	330.23	Calculated Property
λliquid	0.09	W/m×K	359.12	Calculated Property
λliquid	0.09	W/m×K	388.01	Calculated Property
λliquid	0.08	W/m×K	416.90	Calculated Property

Similar Compounds

Find more compounds similar to Ethane, 1,1-dichloro-.

Mixtures

• Ethane, 1,1-dichloro- + Water
• Ethane, 1,1-dichloro- + 1,3,5,7-Tetraazabicyclo[3.3.1]nonane, 3,7-dinitroso-

Sources

• KDB Vapor Pressure Data
• Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 ChEDL chemicals 1.5.2, from Marsh, K. N.; Abramson, A.; Ambrose, D.; Morton, D. W.; Nikitin, E.; Tsonopoulos, C.; Young, C. L. Vapor-Liquid Critical Properties of Elements and Compounds. 10. Organic Compounds Containing Halogens. J. Chem. Eng. Data 2007, 52, 1509-1538.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Solubility of 3,7-Dinitro-1,3,5,7-tetraazabicyclo [3.3.1] Nonane in Ethanenitrile, Methanol, 1,1-Dichloroethane, Dimethyl Sulfoxide, Acetone, and Mixed Solvents
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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