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_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. 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	[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	Outlier 455.00		NIST
Inp	430.00		NIST
Inp	441.00		NIST
Inp	414.00		NIST
Inp	432.00		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	134.40	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	[134.82; 134.82]	K
Ttriple	134.82 ± 0.02	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,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	[61.31; 130.78]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			1.39610e+01
Coefficient B			2.00620e-01
Coefficient C			-1.05400e-04
Coefficient D			2.16000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	61.31	J/mol×K	273.00	Calculated Property
Cp,gas	72.70	J/mol×K	353.78	Calculated Property
Cp,gas	83.01	J/mol×K	434.56	Calculated Property
Cp,gas	92.31	J/mol×K	515.33	Calculated Property
Cp,gas	100.67	J/mol×K	596.11	Calculated Property
Cp,gas	108.17	J/mol×K	676.89	Calculated Property
Cp,gas	114.85	J/mol×K	757.67	Calculated Property
Cp,gas	120.81	J/mol×K	838.44	Calculated Property
Cp,gas	126.09	J/mol×K	919.22	Calculated Property
Cp,gas	130.78	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0030588; 0.0001686]	Pa×s	[134.62; 322.26]	Joback Predicted correlation
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.07671e+01
Coefficient B			6.70080e+02
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			134.62
Temperature range, max.			322.26
η	0.0030588	Pa×s	134.62	Calculated Property
η	0.0015692	Pa×s	155.47	Calculated Property
η	0.0009427	Pa×s	176.32	Calculated Property
η	0.0006307	Pa×s	197.17	Calculated Property
η	0.0004557	Pa×s	218.02	Calculated Property
η	0.0003485	Pa×s	238.87	Calculated Property
η	0.0002782	Pa×s	259.72	Calculated Property
η	0.0002297	Pa×s	280.57	Calculated Property
η	0.0001947	Pa×s	301.41	Calculated Property
η	0.0001686	Pa×s	322.26	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	[1.74e-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
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
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

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 + 2-Methyl-1-butanol
• 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
• 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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