Trichloromonofluoromethane (CAS 75-69-4)

InChI

InChI=1S/CCl3F/c2-1(3,4)5

InChI Key

CYRMSUTZVYGINF-UHFFFAOYSA-N

Formula

CCl3F

SMILES

FC(Cl)(Cl)Cl

Molecular Weight¹

137.37

CAS

75-69-4

Other Names

Algofrene Type 1
Arcton 11
Arcton 9
CCl3F
CFCl3
Chladone 11
Chlorofluoromethane (CCl3F)
Daiflon 11
Daiflon S 1
Distillex DS6
Dymel 11
Electro-CF 11
F 11
F 11 (halocarbon)
F 11B
FC 11
FC 11, Halocarbon
FKW 11
Fluon 11
Fluorocarbon 11
Fluorochloroform
Freon 11
Freon 11A
Freon MF
Frigen 11
Frigen 11A
Frigen S 11
Genetron 11
Genetron 11SBA
Halon 11
Isceon 131
Isotron 11
Kaltron 11
Khladon 11
Ledon 11
Methane, fluorotrichloro-
Methane, trichlorofluoro-
Monofluorotrichloromethane
Propellant 11
R 11
R 11, Halocarbon
R-11
REFRIGERANT-11
Refrigerant 11
Refrigerant R11
Trichlorofluorocarbon
Trichloromethyl fluoride
Triclorofluormethane
fluorotrichloromethane
trichlorofluoromethane

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).
EA : Electron affinity (eV).
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.
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.

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Physical Properties

Property	Value	Unit	Source
ω	0.1890		KDB
μ	0.50	debye	KDB
EA	[1.02; 1.10]	eV
EA	1.02	eV	NIST
EA	1.10 ± 0.30	eV	NIST
Δ_fG°	-245.50	kJ/mol	KDB
Δ_fH°_gas	[-290.00; -268.30]	kJ/mol
Δ_fH°_gas	-284.70	kJ/mol	KDB
Δ_fH°_gas	-278.00 ± 8.80	kJ/mol	NIST
Δ_fH°_gas	-268.30 ± 8.40	kJ/mol	NIST
Δ_fH°_gas	-290.00 ± 20.00	kJ/mol	NIST
Δ_fusH°	6.60	kJ/mol	Joback Calculated Property
Δ_vapH°	26.61	kJ/mol	Relay (1.0) Calculated Property
IE	[11.46; 11.90]	eV
IE	11.68 ± 0.13	eV	NIST
IE	11.73 ± 0.02	eV	NIST
IE	Outlier 11.46 ± 0.02	eV	NIST
IE	11.77 ± 0.01	eV	NIST
IE	11.77 ± 0.02	eV	NIST
IE	11.76 ± 0.01	eV	NIST
IE	11.85	eV	NIST
IE	11.90	eV	NIST
log₁₀WS	-2.17		Relay (1.0) Calculated Property
logP_oct/wat	2.284		Crippen Calculated Property
McVol	63.440	ml/mol	McGowan Calculated Property
P_c	[4370.00; 4466.00]	kPa
P_c	4410.00	kPa	KDB
P_c	4466.00 ± 12.00	kPa	NIST
P_c	4370.00 ± 50.00	kPa	NIST
P_c	4405.73	kPa	NIST
ρ_c	[553.59; 570.21]	kg/m³
ρ_c	570.21 ± 0.55	kg/m³	NIST
ρ_c	553.59 ± 5.54	kg/m³	NIST
ρ_c	553.59 ± 1.37	kg/m³	NIST
I_np	[460.00; 486.00]
I_np	486.00		NIST
I_np	470.00		NIST
I_np	485.00		NIST
I_np	486.00		NIST
I_np	482.00		NIST
I_np	Outlier 460.00		NIST
I_np	478.00		NIST
I_np	478.00		NIST
I_np	484.00		NIST
I_np	482.00		NIST
I_np	484.00		NIST
I_np	Outlier 460.00		NIST
I_np	484.00		NIST
I_np	470.00		NIST
I	[605.00; 605.00]
I	605.00		NIST
I	605.00		NIST
S°_liquid	225.60	J/mol×K	NIST
T_boil	[296.80; 296.92]	K
T_boil	296.90	K	KDB
T_boil	296.90	K	NIST
T_boil	296.80 ± 0.05	K	NIST
T_boil	296.92	K	NIST
T_c	[471.10; 471.20]	K
T_c	471.20	K	KDB
T_c	471.10 ± 0.50	K	NIST
T_c	471.15 ± 0.10	K	NIST
T_c	471.15 ± 0.04	K	NIST
T_c	471.15	K	NIST
T_c	471.15 ± 0.40	K	NIST
T_fus	[162.00; 165.40]	K
T_fus	162.04	K	KDB
T_fus	162.00 ± 2.00	K	NIST
T_fus	162.72 ± 0.01	K	NIST
T_fus	162.70 ± 0.10	K	NIST
T_fus	Outlier 165.40 ± 0.20	K	NIST
T_fus	162.67 ± 0.05	K	NIST
T_triple	[162.10; 162.70]	K
T_triple	162.19 ± 0.05	K	NIST
T_triple	162.69 ± 0.06	K	NIST
T_triple	162.67 ± 0.06	K	NIST
T_triple	162.68 ± 0.03	K	NIST
T_triple	162.65 ± 0.02	K	NIST
T_triple	162.69 ± 0.03	K	NIST
T_triple	162.70 ± 0.01	K	NIST
T_triple	Outlier 162.10 ± 0.20	K	NIST
T_triple	162.68 ± 0.07	K	NIST
V_c	[0.247; 0.248]	m³/kmol
V_c	0.248	m³/kmol	KDB
V_c	0.247 ± 0.006	m³/kmol	NIST
Z_c	0.2791570		KDB
Z_ra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[80.39; 95.18]	J/mol×K	[330.81; 525.81]

C_p,gas	80.39	J/mol×K	330.81	Joback Calculated Property
C_p,gas	83.65	J/mol×K	363.31	Joback Calculated Property
C_p,gas	86.57	J/mol×K	395.81	Joback Calculated Property
C_p,gas	89.16	J/mol×K	428.31	Joback Calculated Property
C_p,gas	91.44	J/mol×K	460.81	Joback Calculated Property
C_p,gas	93.44	J/mol×K	493.31	Joback Calculated Property
C_p,gas	95.18	J/mol×K	525.81	Joback Calculated Property
C_p,liquid	[109.50; 129.30]	J/mol×K	[170.00; 350.00]

C_p,liquid	109.50	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
C_p,liquid	110.40	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	111.20	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	112.00	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	112.90	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	113.70	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	114.60	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
C_p,liquid	115.50	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	116.50	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	117.50	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	118.50	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	118.90	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	119.60	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	120.80	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	121.80	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	121.55	J/mol×K	298.15	NIST
C_p,liquid	126.70	J/mol×K	298.15	NIST
C_p,liquid	122.00	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
C_p,liquid	122.50	J/mol×K	303.15	NIST
C_p,liquid	123.30	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
C_p,liquid	124.70	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
C_p,liquid	126.10	J/mol×K	330.00	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	127.70	J/mol×K	340.00	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	129.30	J/mol×K	350.00	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	[6.89; 7.90]	kJ/mol	[162.68; 165.40]
Δ_fusH	6.89	kJ/mol	162.68	NIST
Δ_fusH	6.90	kJ/mol	162.70	NIST
Δ_fusH	7.90	kJ/mol	165.40	NIST
Δ_vapH	[24.70; 28.50]	kJ/mol	[231.00; 446.00]

Δ_vapH	28.20	kJ/mol	231.00	NIST
Δ_vapH	28.50	kJ/mol	257.00	NIST
Δ_vapH	27.30	kJ/mol	265.00	NIST
Δ_vapH	27.10	kJ/mol	265.00	NIST
Δ_vapH	26.40	kJ/mol	289.00	NIST
Δ_vapH	25.20	kJ/mol	290.00	NIST
Δ_vapH	25.21	kJ/mol	290.40	NIST
Δ_vapH	24.77	kJ/mol	297.10	KDB
Δ_vapH	25.60	kJ/mol	329.00	NIST
Δ_vapH	24.70	kJ/mol	393.00	NIST
Δ_vapH	25.10	kJ/mol	446.00	NIST
ρ_l	1494.00	kg/m³	290.00	KDB
Δ_fusS	[42.38; 47.80]	J/mol×K	[162.68; 165.40]
Δ_fusS	42.38	J/mol×K	162.68	NIST
Δ_fusS	47.80	J/mol×K	165.40	NIST
γ	0.02	N/m	277.60	KDB
Δ_vapS	86.81	J/mol×K	290.40	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 4420.29]	kPa	[214.36; 471.11]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.40921e+01
Coefficient B			-2.49136e+03
Coefficient C			-3.38850e+01
Temperature range, min.			214.36
Temperature range, max.			471.11

P_vap	1.33	kPa	214.36	Calculated Property
P_vap	8.77	kPa	242.89	Calculated Property
P_vap	36.73	kPa	271.42	Calculated Property
P_vap	113.08	kPa	299.94	Calculated Property
P_vap	280.04	kPa	328.47	Calculated Property
P_vap	590.88	kPa	357.00	Calculated Property
P_vap	1104.49	kPa	385.53	Calculated Property
P_vap	1879.56	kPa	414.05	Calculated Property
P_vap	2969.72	kPa	442.58	Calculated Property
P_vap	4420.29	kPa	471.11	Calculated Property
P_vap	[4.88e-03; 4467.78]	kPa	[162.04; 471.20]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + Cln(T) + DT^2
Coefficient A			7.72409e+01
Coefficient B			-5.39795e+03
Coefficient C			-9.73971e+00
Coefficient D			1.15758e-05
Temperature range, min.			162.04
Temperature range, max.			471.20

P_vap	4.88e-03	kPa	162.04	Calculated Property
P_vap	0.29	kPa	196.39	Calculated Property
P_vap	4.33	kPa	230.74	Calculated Property
P_vap	28.32	kPa	265.09	Calculated Property
P_vap	111.85	kPa	299.44	Calculated Property
P_vap	319.38	kPa	333.80	Calculated Property
P_vap	735.39	kPa	368.15	Calculated Property
P_vap	1464.61	kPa	402.50	Calculated Property
P_vap	2643.90	kPa	436.85	Calculated Property
P_vap	4467.78	kPa	471.20	Calculated Property

Similar Compounds

Find more compounds similar to Trichloromonofluoromethane.

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