Chemical Properties of Ethyl Chloride (CAS 75-00-3)

InChI

InChI=1S/C2H5Cl/c1-2-3/h2H2,1H3

InChI Key

HRYZWHHZPQKTII-UHFFFAOYSA-N

Formula

C2H5Cl

SMILES

CCCl

Molecular Weight¹

64.51

CAS

75-00-3

Other Names

• Aethylchlorid
• Aethylis
• Aethylis chloridum
• Anodynon
• C2H5Cl
• Chelen
• Chloorethaan
• Chlorene
• Chlorethyl
• Chloridum
• Chloroaethan
• Chlorure D'ethyle
• Chloryl
• Chloryl anesthetic
• Chloryle anesthetic
• Cloretilo
• Cloroetano
• Cloruro di etile
• Dublofix
• Ether chloratus
• Ether hydrochloric
• Ether muriatic
• Etylu chlorek
• Hydrochloric ether
• Kelene
• Monochlorethane
• Monochloroethane
• Muriatic ether
• NCI-C06224
• Narcotile
• R-160
• UN 1037
• chloroethane
• ethane, chloro-
• freon 160

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_gas : Standard gas 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).
• S_Prot : Protonation entropy at 298K (J/mol×K).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• 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.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.1895; 0.1940]
ω	0.1895		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.1940		ChemSep v8.3 pure component data Compiled value
ω	0.1910		KDB
PAff	[679.50; 693.40]	kJ/mol
PAff	693.40	kJ/mol	NIST
PAff	679.50 ± 1.40	kJ/mol	NIST
Tig	792.04	K	KDB
BasG	[655.60; 666.90]	kJ/mol
BasG	666.90	kJ/mol	NIST
BasG	655.60 ± 1.40	kJ/mol	NIST
ΔcH°gas	[-1430.00; -1413.10]	kJ/mol
ΔcH°gas	-1413.10 ± 0.59	kJ/mol	NIST
ΔcH°gas	-1430.00 ± 10.00	kJ/mol	NIST
μ	[2.00; 2.05]	debye
μ	2.05	debye	ChemSep v8.3 pure component data Compiled value
μ	2.00	debye	KDB
SProt	28.50	J/mol×K	NIST
LFL	3.60	% in Air	KDB
UFL	12.00	% in Air	KDB
Tflash,cc	230.37	K	KDB
Tflash,oc	223.15	K	KDB
ΔfG°	[-60.50; -60.04]	kJ/mol
ΔfG°	-60.50	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-60.04	kJ/mol	KDB
ΔfH°gas	[-112.30; -100.00]	kJ/mol
ΔfH°gas	-111.24 ± 0.22	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	-112.26	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-111.80	kJ/mol	KDB
ΔfH°gas	-112.10 ± 0.70	kJ/mol	NIST
ΔfH°gas	-112.30 ± 0.75	kJ/mol	NIST
ΔfH°gas	-107.70 ± 0.59	kJ/mol	NIST
ΔfH°gas	-109.00 ± 2.00	kJ/mol	NIST
ΔfH°gas	-112.00	kJ/mol	NIST
ΔfH°gas	Outlier -100.00	kJ/mol	NIST
ΔfH°liquid	-137.00 ± 1.00	kJ/mol	NIST
ΔfusH°	5.13	kJ/mol	Joback Calculated Property
ΔvapH°	24.60 ± 0.30	kJ/mol	NIST
IE	[10.95; 11.06]	eV
IE	10.98 ± 0.02	eV	NIST
IE	10.95	eV	NIST
IE	11.04 ± 0.05	eV	NIST
IE	11.00	eV	NIST
IE	10.98 ± 0.02	eV	NIST
IE	10.98 ± 0.01	eV	NIST
IE	10.97 ± 0.02	eV	NIST
IE	11.06	eV	NIST
IE	11.01	eV	NIST
IE	11.01	eV	NIST
IE	11.06 ± 0.02	eV	NIST
IE	11.01	eV	NIST
log10WS	[-1.06; -1.06]
log10WS	-1.06		Aq. Solubility Prediction
log10WS	-1.06		Estimated Solubility
logPoct/wat	1.245		Crippen Calculated Property
McVol	51.280	ml/mol	McGowan Calculated Property
NFPA Fire	4		KDB
NFPA Health	2		KDB
Pc	[5200.00; 5300.00]	kPa
Pc	5200.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Pc	5268.90	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	5300.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	5300.00	kPa	KDB
Pc	5240.53 ± 40.53	kPa	NIST
Ptriple	1.25e-04	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[414.00; 455.00]
Inp	441.00		NIST
Inp	431.00		NIST
Inp	431.00		NIST
Inp	431.00		NIST
Inp	416.00		NIST
Inp	414.00		NIST
Inp	415.00		NIST
Inp	416.00		NIST
Inp	417.00		NIST
Inp	427.00		NIST
Inp	432.00		NIST
Inp	423.96		NIST
Inp	424.09		NIST
Inp	424.00		NIST
Inp	Outlier 455.00		NIST
Inp	430.00		NIST
Inp	434.00		NIST
Inp	446.00		NIST
Inp	432.00		NIST
Inp	430.00		NIST
Inp	430.00		NIST
Inp	430.00		NIST
Inp	426.00		NIST
Inp	430.00		NIST
Inp	432.00		NIST
Inp	426.00		NIST
Inp	447.00		NIST
Inp	447.00		NIST
Inp	Outlier 455.00		NIST
Inp	430.00		NIST
Inp	441.00		NIST
Inp	414.00		NIST
Inp	432.00		NIST
Ip	[661.08; 668.00]
Ip	668.00		NIST
Ip	661.08		NIST
Ip	661.45		NIST
Ip	661.48		NIST
Ip	668.00		NIST
Ip	668.00		NIST
S°liquid	186.27	J/mol×K	NIST
Tboil	[285.42; 307.90]	K
Tboil	285.42	K	ChemSep v8.3 pure component data Compiled value
Tboil	286.20	K	KDB
Tboil	285.50	K	NIST
Tboil	287.10 ± 0.30	K	NIST
Tboil	286.05 ± 0.50	K	NIST
Tboil	286.25 ± 0.60	K	NIST
Tboil	285.45 ± 0.20	K	NIST
Tboil	286.00 ± 0.50	K	NIST
Tboil	Outlier 307.90 ± 0.70	K	NIST
Tboil	287.20 ± 0.20	K	NIST
Tc	[460.00; 460.40]	K
Tc	460.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Tc	460.40	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	460.30	K	ChemSep v8.3 pure component data Compiled value
Tc	460.40	K	KDB
Tc	460.35 ± 0.40	K	NIST
Tfus	[132.30; 137.00]	K
Tfus	134.30	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	136.75	K	ChemSep v8.3 pure component data Compiled value
Tfus	134.40	K	KDB
Tfus	134.30	K	Aq. Solubility Prediction
Tfus	136.75 ± 0.40	K	NIST
Tfus	133.00 ± 2.00	K	NIST
Tfus	137.00 ± 0.50	K	NIST
Tfus	132.30 ± 0.20	K	NIST
Ttriple	[134.80; 134.82]	K
Ttriple	134.81	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	134.80	K	ChemSep v8.3 pure component data Compiled value
Ttriple	134.82 ± 0.02	K	NIST
Ttriple	134.82 ± 0.02	K	NIST
UQi	2.11		ChemSep v8.3 pure component data Compiled value
URi	2.37		ChemSep v8.3 pure component data Compiled value
Vc	[0.199; 0.199]	m3/kmol
Vc	0.199	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.199	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.199	m3/kmol	KDB
Zc	[0.2755220; 0.2760000]
Zc	0.2760000		ChemSep v8.3 pure component data Compiled value
Zc	0.2755220		KDB
Zra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[95.56; 115.00]	J/mol×K	[140.00; 320.00]
Cp,liquid	96.91	J/mol×K	140.00	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	96.34	J/mol×K	150.00	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	95.93	J/mol×K	160.00	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	95.67	J/mol×K	170.00	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	95.56	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	95.60	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	95.77	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	96.09	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	96.55	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	97.14	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	97.87	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	98.73	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	99.72	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	101.00	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	101.00	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	102.00	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	109.60	J/mol×K	288.00	NIST
Cp,liquid	104.00	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	103.30	J/mol×K	290.00	NIST
Cp,liquid	108.80	J/mol×K	298.00	NIST
Cp,liquid	107.70	J/mol×K	298.00	NIST
Cp,liquid	108.80	J/mol×K	298.10	NIST
Cp,liquid	106.00	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	107.00	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
Cp,liquid	110.00	J/mol×K	310.00	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	115.00	J/mol×K	320.00	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	[4.45; 4.45]	kJ/mol	[134.80; 134.82]
ΔfusH	4.45	kJ/mol	134.80	NIST
ΔfusH	4.45	kJ/mol	134.80	NIST
ΔfusH	4.45	kJ/mol	134.82	NIST
ΔfusH	4.45	kJ/mol	134.82	NIST
ΔvapH	[24.40; 27.80]	kJ/mol	[251.50; 431.50]
ΔvapH	25.90	kJ/mol	251.50	NIST
ΔvapH	25.90	kJ/mol	251.50	NIST
ΔvapH	27.80	kJ/mol	256.00	NIST
ΔvapH	24.65	kJ/mol	285.42	NIST
ΔvapH	24.65	kJ/mol	285.42	NIST
ΔvapH	24.69	kJ/mol	285.50	KDB
ΔvapH	24.83	kJ/mol	294.00	NIST
ΔvapH	25.10	kJ/mol	314.50	NIST
ΔvapH	24.40	kJ/mol	373.50	NIST
ΔvapH	24.40	kJ/mol	431.50	NIST
ρl	896.00	kg/m3	293.00	KDB
ΔfusS	[33.02; 33.02]	J/mol×K	[134.82; 134.82]
ΔfusS	33.02	J/mol×K	134.82	NIST
ΔfusS	33.02	J/mol×K	134.82	NIST
γ	0.02	N/m	283.20	KDB
ΔvapS	[86.37; 86.37]	J/mol×K	[285.42; 285.42]
ΔvapS	86.37	J/mol×K	285.42	NIST
ΔvapS	86.37	J/mol×K	285.42	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[12.77; 150.98]	J/mol×K	[10.00; 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			1.27660e+01
Coefficient B			-1.17095e+02
Coefficient C			4.13365e+00
Coefficient D			1.11696e-03
Coefficient E			-3.56556e-07
Temperature range, min.			10.00
Temperature range, max.			1500.00
Cp,gas	12.77	J/mol×K	10.00	Calculated Property
Cp,gas	51.31	J/mol×K	175.56	Calculated Property
Cp,gas	74.94	J/mol×K	341.11	Calculated Property
Cp,gas	92.36	J/mol×K	506.67	Calculated Property
Cp,gas	107.32	J/mol×K	672.22	Calculated Property
Cp,gas	120.47	J/mol×K	837.78	Calculated Property
Cp,gas	131.72	J/mol×K	1003.33	Calculated Property
Cp,gas	140.75	J/mol×K	1168.89	Calculated Property
Cp,gas	147.26	J/mol×K	1334.44	Calculated Property
Cp,gas	150.98	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[95.95; 117.09]	J/mol×K	[134.80; 340.00]	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			9.59460e+01
Coefficient B			-7.24700e+03
Coefficient C			6.05612e+01
Coefficient D			-1.66960e-01
Coefficient E			1.77950e-04
Temperature range, min.			134.80
Temperature range, max.			340.00
Cp,liquid	95.95	J/mol×K	134.80	Calculated Property
Cp,liquid	95.95	J/mol×K	157.60	Calculated Property
Cp,liquid	95.97	J/mol×K	180.40	Calculated Property
Cp,liquid	96.13	J/mol×K	203.20	Calculated Property
Cp,liquid	96.81	J/mol×K	226.00	Calculated Property
Cp,liquid	98.43	J/mol×K	248.80	Calculated Property
Cp,liquid	101.20	J/mol×K	271.60	Calculated Property
Cp,liquid	105.11	J/mol×K	294.40	Calculated Property
Cp,liquid	110.23	J/mol×K	317.20	Calculated Property
Cp,liquid	117.09	J/mol×K	340.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0027471; 0.0001197]	Pa×s	[150.00; 433.00]	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			-1.00650e+01
Coefficient B			6.98320e+02
Coefficient C			-9.76910e-02
Coefficient D			8.00180e-08
Coefficient E			2.00000e+00
Temperature range, min.			150.00
Temperature range, max.			433.00
η	0.0027471	Pa×s	150.00	Calculated Property
η	0.0012044	Pa×s	181.44	Calculated Property
η	0.0006723	Pa×s	212.89	Calculated Property
η	0.0004354	Pa×s	244.33	Calculated Property
η	0.0003110	Pa×s	275.78	Calculated Property
η	0.0002378	Pa×s	307.22	Calculated Property
η	0.0001911	Pa×s	338.67	Calculated Property
η	0.0001593	Pa×s	370.11	Calculated Property
η	0.0001366	Pa×s	401.56	Calculated Property
η	0.0001197	Pa×s	433.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[29.80; 10.17]	kJ/mol	[134.80; 443.22]	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			3.61548e+01
Coefficient B			9.81924e-01
Coefficient C			-2.02605e+00
Coefficient D			2.20581e+00
Coefficient E			-7.74155e-01
Critical temperature, Tc (K)			4.60300e+02
Temperature range, min.			134.80
Temperature range, max.			443.22
ΔvapH	29.80	kJ/mol	134.80	Calculated Property
ΔvapH	28.80	kJ/mol	169.07	Calculated Property
ΔvapH	27.80	kJ/mol	203.34	Calculated Property
ΔvapH	26.70	kJ/mol	237.61	Calculated Property
ΔvapH	25.40	kJ/mol	271.88	Calculated Property
ΔvapH	23.80	kJ/mol	306.14	Calculated Property
ΔvapH	21.78	kJ/mol	340.41	Calculated Property
ΔvapH	19.19	kJ/mol	374.68	Calculated Property
ΔvapH	15.71	kJ/mol	408.95	Calculated Property
ΔvapH	10.17	kJ/mol	443.22	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 4110.99]	kPa	[206.18; 460.35]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39805e+01
Coefficient B			-2.45158e+03
Coefficient C			-2.71410e+01
Temperature range, min.			206.18
Temperature range, max.			460.35
Pvap	1.33	kPa	206.18	Calculated Property
Pvap	8.61	kPa	234.42	Calculated Property
Pvap	35.57	kPa	262.66	Calculated Property
Pvap	108.41	kPa	290.90	Calculated Property
Pvap	266.35	kPa	319.14	Calculated Property
Pvap	558.47	kPa	347.39	Calculated Property
Pvap	1038.55	kPa	375.63	Calculated Property
Pvap	1759.80	kPa	403.87	Calculated Property
Pvap	2770.47	kPa	432.11	Calculated Property
Pvap	4110.99	kPa	460.35	Calculated Property
Pvap	[1.63e-04; 5331.79]	kPa	[134.80; 460.30]	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			4.43757e+01
Coefficient B			-4.20639e+03
Coefficient C			-4.47884e+00
Coefficient D			3.81282e-06
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 460.35 K.
Temperature range, min.			134.80
Temperature range, max.			460.30
Pvap	1.63e-04	kPa	134.80	Calculated Property
Pvap	0.04	kPa	170.97	Calculated Property
Pvap	1.41	kPa	207.13	Calculated Property
Pvap	14.95	kPa	243.30	Calculated Property
Pvap	80.90	kPa	279.47	Calculated Property
Pvap	285.67	kPa	315.63	Calculated Property
Pvap	758.29	kPa	351.80	Calculated Property
Pvap	1651.46	kPa	387.97	Calculated Property
Pvap	3123.60	kPa	424.13	Calculated Property
Pvap	5331.79	kPa	460.30	Calculated Property
Pvap	[1.74e-04; 5332.52]	kPa	[136.75; 460.35]	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			6.25703e+01
Coefficient B			-4.77239e+03
Coefficient C			-7.41963e+00
Coefficient D			8.84845e-06
Coefficient E			0.00000e+00
Temperature range, min.			136.75
Temperature range, max.			460.35
Pvap	1.74e-04	kPa	136.75	Calculated Property
Pvap	0.05	kPa	172.71	Calculated Property
Pvap	1.58	kPa	208.66	Calculated Property
Pvap	16.19	kPa	244.62	Calculated Property
Pvap	84.29	kPa	280.57	Calculated Property
Pvap	287.63	kPa	316.53	Calculated Property
Pvap	745.63	kPa	352.48	Calculated Property
Pvap	1607.64	kPa	388.44	Calculated Property
Pvap	3056.99	kPa	424.39	Calculated Property
Pvap	5332.52	kPa	460.35	Calculated Property
Pvap	[2.98; 102.33]	kPa	[217.21; 285.66]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41881e+01
Coefficient B			-2.42421e+03
Coefficient C			-3.20780e+01
Reference			Gordon and Giauque, 1948
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			217.21
Temperature range, max.			285.66
Pvap	2.98	kPa	217.21	Calculated Property
Pvap	5.00	kPa	224.82	Calculated Property
Pvap	8.07	kPa	232.42	Calculated Property
Pvap	12.56	kPa	240.03	Calculated Property
Pvap	18.95	kPa	247.63	Calculated Property
Pvap	27.80	kPa	255.24	Calculated Property
Pvap	39.77	kPa	262.84	Calculated Property
Pvap	55.60	kPa	270.45	Calculated Property
Pvap	76.14	kPa	278.05	Calculated Property
Pvap	102.33	kPa	285.66	Calculated Property
Pvap	[2.98; 102.33]	kPa	[217.21; 285.66]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41881e+01
Coefficient B			-2.42421e+03
Coefficient C			-3.20780e+01
Reference			Gordon and Giauque, 1948, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			217.21
Temperature range, max.			285.66
Pvap	2.98	kPa	217.21	Calculated Property
Pvap	5.00	kPa	224.82	Calculated Property
Pvap	8.07	kPa	232.42	Calculated Property
Pvap	12.56	kPa	240.03	Calculated Property
Pvap	18.95	kPa	247.63	Calculated Property
Pvap	27.80	kPa	255.24	Calculated Property
Pvap	39.77	kPa	262.84	Calculated Property
Pvap	55.60	kPa	270.45	Calculated Property
Pvap	76.14	kPa	278.05	Calculated Property
Pvap	102.33	kPa	285.66	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1084.02; 374.10]	kg/m3	[134.80; 460.30]	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			8.74360e+01
Coefficient B			2.68950e-01
Coefficient C			4.60360e+02
Coefficient D			2.49940e-01
Comment			Range stopped at Tc; ChemSep gives it to 460.35 K.
Temperature range, min.			134.80
Temperature range, max.			460.30
ρl	1084.02	kg/m3	134.80	Calculated Property
ρl	1046.81	kg/m3	170.97	Calculated Property
ρl	1007.40	kg/m3	207.13	Calculated Property
ρl	965.25	kg/m3	243.30	Calculated Property
ρl	919.59	kg/m3	279.47	Calculated Property
ρl	869.17	kg/m3	315.63	Calculated Property
ρl	811.88	kg/m3	351.80	Calculated Property
ρl	743.37	kg/m3	387.97	Calculated Property
ρl	651.83	kg/m3	424.13	Calculated Property
ρl	374.10	kg/m3	460.30	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 6.51e-04]	N/m	[134.80; 443.22]	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			-3.68340e-02
Coefficient B			3.31670e+01
Coefficient C			-2.72060e+00
Coefficient D			4.03910e-05
Coefficient E			-3.33910e-06
Temperature range, min.			134.80
Temperature range, max.			443.22
γ	0.04	N/m	134.80	Calculated Property
γ	0.04	N/m	169.07	Calculated Property
γ	0.03	N/m	203.34	Calculated Property
γ	0.03	N/m	237.61	Calculated Property
γ	0.02	N/m	271.88	Calculated Property
γ	0.02	N/m	306.14	Calculated Property
γ	0.01	N/m	340.41	Calculated Property
γ	0.01	N/m	374.68	Calculated Property
γ	0.00	N/m	408.95	Calculated Property
γ	6.51e-04	N/m	443.22	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.08]	W/m×K	[134.80; 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			-1.98300e+01
Coefficient B			2.01450e-01
Coefficient C			-7.28060e+05
Coefficient D			-2.79170e+08
Temperature range, min.			134.80
Temperature range, max.			1000.00
λgas	0.00	W/m×K	134.80	Calculated Property
λgas	0.01	W/m×K	230.93	Calculated Property
λgas	0.01	W/m×K	327.07	Calculated Property
λgas	0.02	W/m×K	423.20	Calculated Property
λgas	0.03	W/m×K	519.33	Calculated Property
λgas	0.04	W/m×K	615.47	Calculated Property
λgas	0.05	W/m×K	711.60	Calculated Property
λgas	0.06	W/m×K	807.73	Calculated Property
λgas	0.07	W/m×K	903.87	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.19; 0.09]	W/m×K	[134.80; 373.15]	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			6.25440e-02
Coefficient B			1.50840e+02
Coefficient C			-4.31820e+00
Coefficient D			1.25990e-02
Coefficient E			-3.17990e-05
Temperature range, min.			134.80
Temperature range, max.			373.15
λliquid	0.19	W/m×K	134.80	Calculated Property
λliquid	0.18	W/m×K	161.28	Calculated Property
λliquid	0.17	W/m×K	187.77	Calculated Property
λliquid	0.16	W/m×K	214.25	Calculated Property
λliquid	0.14	W/m×K	240.73	Calculated Property
λliquid	0.13	W/m×K	267.22	Calculated Property
λliquid	0.12	W/m×K	293.70	Calculated Property
λliquid	0.11	W/m×K	320.18	Calculated Property
λliquid	0.10	W/m×K	346.67	Calculated Property
λliquid	0.09	W/m×K	373.15	Calculated Property

Similar Compounds

Find more compounds similar to Ethyl Chloride.

Mixtures

• Ethyl Chloride + Methyl Alcohol
• 1-Propanol + Ethyl Chloride
• Ethyl Chloride + 2-Propanol
• Ethyl Chloride + 1-Butanol
• Ethyl Chloride + 1-Propanol, 2-methyl-
• 2-Propanol, 2-methyl- + Ethyl Chloride
• Ethyl Chloride + 2-Pentanol
• Ethyl Chloride + 1-Pentanol
• Ethyl Chloride + 3-Pentanol
• Ethyl Chloride + 1-Butanol, 2-methyl-
• Ethyl Chloride + Amylene hydrate
• Ethyl Chloride + 1-Butanol, 3-methyl-
• Ethyl Chloride + Tetrahydropyran
• Ethyl Chloride + Water
• Ethyl Chloride + Allyl alcohol
• Phenol, 2-methyl- + Ethyl Chloride
• Ethyl Chloride + Phenol, 3-methyl-
• Ethyl Chloride + PHENOL, 4-METHYL-
• Ethyl Chloride + 3-Buten-2-ol, 2-methyl-
• 3-Buten-1-ol, 3-methyl- + Ethyl Chloride

Find more mixtures with Ethyl Chloride.

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.
• 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
• Henry's law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
• Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Propen-1-ol
• Henry s Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Methyl-3-buten-2-ol and 3-Methyl-3-buten-1-ol
• Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Styrene
• Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Methylphenol, 3-Methylphenol, and 4-Methylphenol
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Henry s Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethylether, Chloroethane, 1,1-Difluoroethane, and Hexane in Tetrahydropyran
• 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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