Pentafluoroethyl chloride (CAS 76-15-3)

InChI

InChI=1S/C2ClF5/c3-1(4,5)2(6,7)8

InChI Key

RFCAUADVODFSLZ-UHFFFAOYSA-N

Formula

C2ClF5

SMILES

FC(F)(F)C(F)(F)Cl

Molecular Weight¹

154.47

CAS

76-15-3

Other Names

1-chloro-1,1,2,2,2-pentafluoroethane
1-chloropentafluoroethane
CF3CF2Cl
CFC 115
Ethane, 1-chloro-1,1,2,2,2-pentafluoro-
Ethane, chloropentafluoro-
F-115
FC 115
FKW 115
Fluorocarbon 115
Freon 115
Genetron 115
Propellant 115
R 115
R-115
REFRIGERANT-115
chloropentafluoroethane
chloroperfluoroethane
monochloropentafluoroethane
pentafluorochloroethane
perfluoroethyl chloride

ω : Acentric Factor.
C_p,gas : Ideal gas heat capacity (J/mol×K).
C_p,liquid : Liquid phase heat capacity (J/mol×K).
μ : Dipole Moment (debye).
Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
Δ_fH°_gas : 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).
P_c : Critical Pressure (kPa).
P_vap : Vapor pressure (kPa).
ρ_c : Critical density (kg/m³).
ρ_l : Liquid Density (kg/m³).
I_np : Non-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.
¹: Molecular weight from the IUPAC atomic weights tables.

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Physical Properties

Property	Value	Unit	Source
ω	0.2790		KDB
μ	0.30	debye	KDB
Δ_fG°	-1014.34	kJ/mol	Joback Calculated Property
Δ_fH°_gas	-1114.00 ± 10.00	kJ/mol	NIST
Δ_fusH°	5.70	kJ/mol	Joback Calculated Property
Δ_vapH°	18.40	kJ/mol	Relay (1.0) Calculated Property
IE	[12.60; 12.96]	eV
IE	12.60	eV	NIST
IE	12.96	eV	NIST
log₁₀WS	-2.50		Relay (1.0) Calculated Property
logP_oct/wat	2.380		Crippen Calculated Property
McVol	60.130	ml/mol	McGowan Calculated Property
P_c	[3120.00; 3229.00]	kPa
P_c	3229.00	kPa	KDB
P_c	3120.00 ± 8.00	kPa	NIST
P_c	3157.29 ± 7.09	kPa	NIST
ρ_c	[603.96; 613.08]	kg/m³
ρ_c	603.96 ± 4.63	kg/m³	NIST
ρ_c	613.08 ± 1.50	kg/m³	NIST
I_np	270.00		NIST
S°_liquid	248.03	J/mol×K	NIST
T_boil	[235.00; 263.00]	K
T_boil	235.20	K	KDB
T_boil	235.50 ± 0.50	K	NIST
T_boil	235.20	K	NIST
T_boil	235.00 ± 3.00	K	NIST
T_boil	263.00 ± 3.00	K	NIST
T_c	[352.94; 353.20]	K
T_c	353.20	K	KDB
T_c	352.94 ± 0.05	K	NIST
T_c	353.10 ± 0.15	K	NIST
T_fus	173.71	K	KDB
T_triple	[173.71; 173.71]	K
T_triple	173.71	K	KDB
T_triple	173.71 ± 0.05	K	NIST
T_triple	173.71 ± 0.05	K	NIST
V_c	0.252	m³/kmol	KDB
Z_c	0.2770840		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[99.25; 130.23]	J/mol×K	[272.48; 416.43]

C_p,gas	99.25	J/mol×K	272.48	Joback Calculated Property
C_p,gas	105.39	J/mol×K	296.47	Joback Calculated Property
C_p,gas	111.12	J/mol×K	320.46	Joback Calculated Property
C_p,gas	116.46	J/mol×K	344.46	Joback Calculated Property
C_p,gas	121.41	J/mol×K	368.45	Joback Calculated Property
C_p,gas	126.00	J/mol×K	392.44	Joback Calculated Property
C_p,gas	130.23	J/mol×K	416.43	Joback Calculated Property
C_p,liquid	[131.20; 184.40]	J/mol×K	[180.00; 300.00]

C_p,liquid	131.20	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
C_p,liquid	133.20	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
C_p,liquid	135.50	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
C_p,liquid	138.10	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
C_p,liquid	141.00	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
C_p,liquid	144.40	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
C_p,liquid	145.27	J/mol×K	234.04	NIST
C_p,liquid	148.20	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
C_p,liquid	152.60	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
C_p,liquid	157.50	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
C_p,liquid	163.10	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
C_p,liquid	165.10	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
C_p,liquid	169.50	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
C_p,liquid	176.50	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
C_p,liquid	182.90	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
C_p,liquid	184.40	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
Δ_fusH	[1.88; 2.63]	kJ/mol	[80.24; 173.70]
Δ_fusH	2.63	kJ/mol	80.24	NIST
Δ_fusH	1.88	kJ/mol	173.70	NIST
Δ_fusH	1.88	kJ/mol	173.70	NIST
Δ_vapH	[19.40; 20.90]	kJ/mol	[205.50; 332.50]

Δ_vapH	20.90	kJ/mol	205.50	NIST
Δ_vapH	20.90	kJ/mol	205.50	NIST
Δ_vapH	20.90	kJ/mol	206.00	NIST
Δ_vapH	19.40 ± 0.10	kJ/mol	234.00	NIST
Δ_vapH	19.40 ± 0.10	kJ/mol	234.00	NIST
Δ_vapH	19.41	kJ/mol	234.04	NIST
Δ_vapH	19.41	kJ/mol	234.04	NIST
Δ_vapH	19.46	kJ/mol	234.70	KDB
Δ_vapH	20.10	kJ/mol	249.50	NIST
Δ_vapH	19.70	kJ/mol	289.50	NIST
Δ_vapH	19.70	kJ/mol	332.50	NIST
P_vap	[148.60; 2077.50]	kPa	[243.15; 333.15]

P_vap	148.60	kPa	243.15	Measurements of Bubble Point Pressures for the Binary Mixture of Pentafluoroethane with Chloropentafluoroethane
P_vap	219.90	kPa	253.15	Measurements of Bubble Point Pressures for the Binary Mixture of Pentafluoroethane with Chloropentafluoroethane
P_vap	314.60	kPa	263.15	Measurements of Bubble Point Pressures for the Binary Mixture of Pentafluoroethane with Chloropentafluoroethane
P_vap	439.40	kPa	273.15	Measurements of Bubble Point Pressures for the Binary Mixture of Pentafluoroethane with Chloropentafluoroethane
P_vap	594.92	kPa	283.15	Measurements of Bubble Point Pressures for the Binary Mixture of Pentafluoroethane with Chloropentafluoroethane
P_vap	789.30	kPa	293.15	Measurements of Bubble Point Pressures for the Binary Mixture of Pentafluoroethane with Chloropentafluoroethane
P_vap	1028.40	kPa	303.15	Measurements of Bubble Point Pressures for the Binary Mixture of Pentafluoroethane with Chloropentafluoroethane
P_vap	1317.90	kPa	313.15	Measurements of Bubble Point Pressures for the Binary Mixture of Pentafluoroethane with Chloropentafluoroethane
P_vap	1664.90	kPa	323.15	Measurements of Bubble Point Pressures for the Binary Mixture of Pentafluoroethane with Chloropentafluoroethane
P_vap	2077.50	kPa	333.15	Measurements of Bubble Point Pressures for the Binary Mixture of Pentafluoroethane with Chloropentafluoroethane
ρ_l	1260.00	kg/m³	303.00	KDB
Δ_fusS	[10.79; 32.76]	J/mol×K	[80.24; 173.70]
Δ_fusS	32.76	J/mol×K	80.24	NIST
Δ_fusS	10.79	J/mol×K	173.70	NIST
γ	0.01	N/m	298.20	KDB
Δ_vapS	[82.93; 82.93]	J/mol×K	[234.04; 234.04]
Δ_vapS	82.93	J/mol×K	234.04	NIST
Δ_vapS	82.93	J/mol×K	234.04	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 2775.28]	kPa	[168.03; 353.10]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.38962e+01
Coefficient B			-1.96705e+03
Coefficient C			-2.34850e+01
Temperature range, min.			168.03
Temperature range, max.			353.10

P_vap	1.33	kPa	168.03	Calculated Property
P_vap	7.26	kPa	188.59	Calculated Property
P_vap	27.17	kPa	209.16	Calculated Property
P_vap	78.13	kPa	229.72	Calculated Property
P_vap	185.51	kPa	250.28	Calculated Property
P_vap	381.50	kPa	270.85	Calculated Property
P_vap	702.35	kPa	291.41	Calculated Property
P_vap	1185.30	kPa	311.97	Calculated Property
P_vap	1865.78	kPa	332.54	Calculated Property
P_vap	2775.28	kPa	353.10	Calculated Property
P_vap	[2.23; 3180.82]	kPa	[174.00; 353.00]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + Cln(T) + DT^2
Coefficient A			6.94742e+01
Coefficient B			-4.08741e+03
Coefficient C			-8.85890e+00
Coefficient D			1.71756e-05
Temperature range, min.			174.00
Temperature range, max.			353.00

P_vap	2.23	kPa	174.00	Calculated Property
P_vap	10.77	kPa	193.89	Calculated Property
P_vap	37.03	kPa	213.78	Calculated Property
P_vap	99.88	kPa	233.67	Calculated Property
P_vap	225.62	kPa	253.56	Calculated Property
P_vap	446.93	kPa	273.44	Calculated Property
P_vap	802.34	kPa	293.33	Calculated Property
P_vap	1337.24	kPa	313.22	Calculated Property
P_vap	2106.78	kPa	333.11	Calculated Property
P_vap	3180.82	kPa	353.00	Calculated Property

Similar Compounds

Ethane, 1,2-dichloro-1,1,2,2-tetrafluoro-.

Ethane, 1,1-dichloro-1,2,2,2-tetrafluoro-.

Ethane, 1,1,2-trichloro-1,2,2-trifluoro-.

Ethane, 1,1,1,2-tetrachloro-2,2-difluoro-.

1-Propene, 3-chloro-1,1,2,3,3-pentafluoro-.

1,2-Dichloro-1,1,2,3,3,3-hexafluoropropane.

Find more compounds similar to Pentafluoroethyl chloride.

Mixtures

Ethane, pentafluoro- + Pentafluoroethyl chloride

Sources

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