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
• Chloroethane
• Chlorure D'ethyle
• Chloryl
• Chloryl anesthetic
• Chloryle anesthetic
• Cloretilo
• Cloroetano
• Cloruro di etile
• Dublofix
• Ethane, chloro-
• Ether chloratus
• Ether hydrochloric
• Ether muriatic
• Etylu chlorek
• Hydrochloric ether
• Kelene
• Monochlorethane
• Monochloroethane
• Muriatic ether
• NCI-C06224
• Narcotile
• R-160
• UN 1037
• 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_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : 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).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• 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	0.1910		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	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°	-60.04	kJ/mol	KDB
ΔfH°gas	[-112.30; -100.00]	kJ/mol
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. Sol...
log10WS	-1.06		Estimat...
logPoct/wat	1.245		Crippen Calculated Property
McVol	51.280	ml/mol	McGowan Calculated Property
NFPA Fire	4		KDB
NFPA Health	2		KDB
Pc	[5240.53; 5300.00]	kPa
Pc	5300.00	kPa	KDB
Pc	5240.53 ± 40.53	kPa	NIST
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	441.00		NIST
Inp	414.00		NIST
Inp	432.00		NIST
Inp	430.00		NIST
Inp	Outlier 455.00		NIST
I	[661.08; 668.00]
I	668.00		NIST
I	661.08		NIST
I	661.45		NIST
I	661.48		NIST
I	668.00		NIST
I	668.00		NIST
S°liquid	186.27	J/mol×K	NIST
Tboil	[285.45; 307.90]	K
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	[460.35; 460.40]	K
Tc	460.40	K	KDB
Tc	460.35 ± 0.40	K	NIST
Tfus	[132.30; 137.00]	K
Tfus	134.30	K	Aq. Sol...
Tfus	134.40	K	KDB
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	134.82 ± 0.02	K	NIST
Vc	0.199	m3/kmol	KDB
Zc	0.2755220		KDB
Zra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[62.72; 85.20]	J/mol×K	[282.59; 452.81]
T(K) Ideal gas heat capacity (J/mol×K) 65 70 75 80 85 300 350 400 450
Cp,gas	62.72	J/mol×K	282.59	Joback Calculated Property
Cp,gas	66.80	J/mol×K	310.96	Joback Calculated Property
Cp,gas	70.74	J/mol×K	339.33	Joback Calculated Property
Cp,gas	74.55	J/mol×K	367.70	Joback Calculated Property
Cp,gas	78.23	J/mol×K	396.07	Joback Calculated Property
Cp,gas	81.78	J/mol×K	424.44	Joback Calculated Property
Cp,gas	85.20	J/mol×K	452.81	Joback Calculated Property
Cp,liquid	[103.30; 109.60]	J/mol×K	[288.00; 298.10]
T(K) Liquid phase heat capacity (J/mol×K) 103 104 105 106 107 108 109 110 290 295
Cp,liquid	109.60	J/mol×K	288.00	NIST
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
η	[0.0002258; 0.0023449]	Pa×s	[142.22; 282.59]
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 150 200 250
η	0.0023449	Pa×s	142.22	Joback Calculated Property
η	0.0012052	Pa×s	165.62	Joback Calculated Property
η	0.0007304	Pa×s	189.01	Joback Calculated Property
η	0.0004943	Pa×s	212.41	Joback Calculated Property
η	0.0003615	Pa×s	235.80	Joback Calculated Property
η	0.0002797	Pa×s	259.20	Joback Calculated Property
η	0.0002258	Pa×s	282.59	Joback Calculated Property
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
ΔvapH	[24.40; 27.80]	kJ/mol	[251.50; 431.50]
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 24.5 25 25.5 26 26.5 27 27.5 28 250 300 350 400
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	24.69	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	J/mol×K	134.82	NIST
γ	0.02	N/m	283.20	KDB
ΔvapS	86.37	J/mol×K	285.42	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 4110.99]	kPa	[206.18; 460.35]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
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
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 300 400
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	[1.74e-04; 5332.52]	kPa	[136.75; 460.35]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			6.25703e+01
Coefficient B			-4.77239e+03
Coefficient C			-7.41963e+00
Coefficient D			8.84845e-06
Temperature range, min.			136.75
Temperature range, max.			460.35
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 200 300 400
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

Similar Compounds

Find more compounds similar to Ethyl Chloride.

Mixtures

• Ethyl Chloride + Tetrahydropyran
• Ethyl Chloride + Methyl Alcohol
• 1-Propanol + Ethyl Chloride
• Ethyl Chloride + Isopropyl Alcohol
• 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 + 2-Methyl-1-butanol
• Ethyl Chloride + Amylene hydrate
• Ethyl Chloride + 1-Butanol, 3-methyl-
• Ethyl Chloride + 2-Propen-1-ol
• Ethyl Chloride + 3-Buten-2-ol, 2-methyl-
• 3-Buten-1-ol, 3-methyl- + Ethyl Chloride
• Benzene + Ethyl Chloride
• Toluene + Ethyl Chloride
• Ethyl Chloride + o-Xylene
• Ethyl Chloride + Benzene, 1,3-dimethyl-

Find more mixtures with Ethyl Chloride.

Sources

• KDB Vapor Pressure Data
• 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

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Outlier This icon means that the value is more than 2 standard deviations away from the property mean.