Chemical Properties of 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).
• η : Dynamic viscosity (Pa×s).
• EA : Electron affinity (eV).
• ε_r : Dielectric Constant (Relative permittivity).
• 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).
• n₀ : Refractive Index.
• 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.

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
εr	2.30		NCMS SOLV-DB
ΔfG°	-245.50	kJ/mol	KDB
ΔfH°gas	[-290.00; -268.30]	kJ/mol
ΔfH°gas	-284.70	kJ/mol	KDB
ΔfH°gas	-278.00 ± 8.80	kJ/mol	NIST
ΔfH°gas	-268.30 ± 8.40	kJ/mol	NIST
ΔfH°gas	-290.00 ± 20.00	kJ/mol	NIST
ΔfusH°	6.60	kJ/mol	Joback Calculated Property
ΔvapH°	25.02	kJ/mol	NCMS SOLV-DB
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
logPoct/wat	2.530		NCMS SOLV-DB
McVol	63.440	ml/mol	McGowan Calculated Property
Pc	[4370.00; 4466.00]	kPa
Pc	4410.00	kPa	KDB
Pc	4466.00 ± 12.00	kPa	NIST
Pc	4370.00 ± 50.00	kPa	NIST
Pc	4405.73	kPa	NIST
ρc	[553.59; 570.21]	kg/m3
ρc	570.21 ± 0.55	kg/m3	NIST
ρc	553.59 ± 5.54	kg/m3	NIST
ρc	553.59 ± 1.37	kg/m3	NIST
Inp	[460.00; 486.00]
Inp	486.00		NIST
Inp	470.00		NIST
Inp	485.00		NIST
Inp	486.00		NIST
Inp	482.00		NIST
Inp	Outlier 460.00		NIST
Inp	478.00		NIST
Inp	478.00		NIST
Inp	484.00		NIST
Inp	482.00		NIST
Inp	484.00		NIST
Inp	Outlier 460.00		NIST
Inp	484.00		NIST
Inp	470.00		NIST
I	[605.00; 605.00]
I	605.00		NIST
I	605.00		NIST
S°liquid	225.60	J/mol×K	NIST
Tboil	[296.78; 296.92]	K
Tboil	296.90	K	KDB
Tboil	296.78	K	NCMS SOLV-DB
Tboil	296.90	K	NIST
Tboil	296.80 ± 0.05	K	NIST
Tboil	296.92	K	NIST
Tc	[471.10; 471.20]	K
Tc	471.20	K	KDB
Tc	471.10 ± 0.50	K	NIST
Tc	471.15 ± 0.10	K	NIST
Tc	471.15 ± 0.04	K	NIST
Tc	471.15	K	NIST
Tc	471.15 ± 0.40	K	NIST
Tfus	[162.00; 165.40]	K
Tfus	162.04	K	KDB
Tfus	162.67	K	NCMS SOLV-DB
Tfus	162.00 ± 2.00	K	NIST
Tfus	162.72 ± 0.01	K	NIST
Tfus	162.70 ± 0.10	K	NIST
Tfus	Outlier 165.40 ± 0.20	K	NIST
Tfus	162.67 ± 0.05	K	NIST
Ttriple	[162.10; 162.70]	K
Ttriple	162.19 ± 0.05	K	NIST
Ttriple	162.69 ± 0.06	K	NIST
Ttriple	162.67 ± 0.06	K	NIST
Ttriple	162.68 ± 0.03	K	NIST
Ttriple	162.65 ± 0.02	K	NIST
Ttriple	162.69 ± 0.03	K	NIST
Ttriple	162.70 ± 0.01	K	NIST
Ttriple	Outlier 162.10 ± 0.20	K	NIST
Ttriple	162.68 ± 0.07	K	NIST
Vc	[0.247; 0.248]	m3/kmol
Vc	0.248	m3/kmol	KDB
Vc	0.247 ± 0.006	m3/kmol	NIST
Zc	0.2791570		KDB
Zra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[109.50; 129.30]	J/mol×K	[170.00; 350.00]
Cp,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
Cp,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
Cp,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
Cp,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
Cp,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
Cp,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
Cp,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
Cp,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
Cp,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
Cp,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
Cp,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
Cp,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
Cp,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
Cp,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
Cp,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
Cp,liquid	121.55	J/mol×K	298.15	NIST
Cp,liquid	126.70	J/mol×K	298.15	NIST
Cp,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
Cp,liquid	122.50	J/mol×K	303.15	NIST
Cp,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
Cp,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
Cp,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
Cp,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
Cp,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
η	0.0004430	Pa×s	298.15	NCMS SOLV-DB
ΔfusH	[6.89; 7.90]	kJ/mol	[162.68; 165.40]
ΔfusH	6.89	kJ/mol	162.68	NIST
ΔfusH	6.90	kJ/mol	162.70	NIST
ΔfusH	7.90	kJ/mol	165.40	NIST
ΔvapH	[24.70; 28.50]	kJ/mol	[231.00; 446.00]
ΔvapH	28.20	kJ/mol	231.00	NIST
ΔvapH	28.50	kJ/mol	257.00	NIST
ΔvapH	27.30	kJ/mol	265.00	NIST
ΔvapH	27.10	kJ/mol	265.00	NIST
ΔvapH	26.40	kJ/mol	289.00	NIST
ΔvapH	25.20	kJ/mol	290.00	NIST
ΔvapH	25.21	kJ/mol	290.40	NIST
ΔvapH	24.77	kJ/mol	297.10	KDB
ΔvapH	25.60	kJ/mol	329.00	NIST
ΔvapH	24.70	kJ/mol	393.00	NIST
ΔvapH	25.10	kJ/mol	446.00	NIST
Pvap	107.06	kPa	298.15	NCMS SOLV-DB
n0	1.37900		298.15	NCMS SOLV-DB
ρl	1494.00	kg/m3	290.00	KDB
ΔfusS	[42.38; 47.80]	J/mol×K	[162.68; 165.40]
ΔfusS	42.38	J/mol×K	162.68	NIST
ΔfusS	47.80	J/mol×K	165.40	NIST
γ	[0.02; 0.02]	N/m	[277.60; 298.15]
γ	0.02	N/m	277.60	KDB
γ	0.02	N/m	298.15	NCMS SOLV-DB
ΔvapS	86.81	J/mol×K	290.40	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[78.00; 96.75]	J/mol×K	[298.00; 600.00]	NIST
Equation			Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,gas in J/mol×K, T in K
Coefficient A			3.40665e+01
Coefficient B			2.30431e+02
Coefficient C			-2.89456e+02
Coefficient D			1.35525e+02
Coefficient E			-2.32263e-01
Reference			Chase, 1998
Comment			F=-307.5847, G=292.6202, H=-288.6964; Data last reviewed in June, 1970
Temperature range, min.			298.00
Temperature range, max.			600.00
Cp,gas	78.00	J/mol×K	298.00	Calculated Property
Cp,gas	81.47	J/mol×K	331.56	Calculated Property
Cp,gas	84.47	J/mol×K	365.11	Calculated Property
Cp,gas	87.05	J/mol×K	398.67	Calculated Property
Cp,gas	89.29	J/mol×K	432.22	Calculated Property
Cp,gas	91.22	J/mol×K	465.78	Calculated Property
Cp,gas	92.90	J/mol×K	499.33	Calculated Property
Cp,gas	94.35	J/mol×K	532.89	Calculated Property
Cp,gas	95.63	J/mol×K	566.44	Calculated Property
Cp,gas	96.75	J/mol×K	600.00	Calculated Property
Cp,gas	[96.61; 108.00]	J/mol×K	[600.00; 6000.00]	NIST
Equation			Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,gas in J/mol×K, T in K
Coefficient A			1.06269e+02
Coefficient B			1.24528e+00
Coefficient C			-2.92652e-01
Coefficient D			2.26580e-02
Coefficient E			-3.71008e+00
Reference			Chase, 1998
Comment			F=-331.8887, G=419.8728, H=-288.6964; Data last reviewed in June, 1970
Temperature range, min.			600.00
Temperature range, max.			6000.00
Cp,gas	96.61	J/mol×K	600.00	Calculated Property
Cp,gas	104.81	J/mol×K	1200.00	Calculated Property
Cp,gas	106.55	J/mol×K	1800.00	Calculated Property
Cp,gas	107.24	J/mol×K	2400.00	Calculated Property
Cp,gas	107.57	J/mol×K	3000.00	Calculated Property
Cp,gas	107.73	J/mol×K	3600.00	Calculated Property
Cp,gas	107.81	J/mol×K	4200.00	Calculated Property
Cp,gas	107.85	J/mol×K	4800.00	Calculated Property
Cp,gas	107.90	J/mol×K	5400.00	Calculated Property
Cp,gas	108.00	J/mol×K	6000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 4420.29]	kPa	[214.36; 471.11]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
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
Pvap	1.33	kPa	214.36	Calculated Property
Pvap	8.77	kPa	242.89	Calculated Property
Pvap	36.73	kPa	271.42	Calculated Property
Pvap	113.08	kPa	299.94	Calculated Property
Pvap	280.04	kPa	328.47	Calculated Property
Pvap	590.88	kPa	357.00	Calculated Property
Pvap	1104.49	kPa	385.53	Calculated Property
Pvap	1879.56	kPa	414.05	Calculated Property
Pvap	2969.72	kPa	442.58	Calculated Property
Pvap	4420.29	kPa	471.11	Calculated Property
Pvap	[4.88e-03; 4467.78]	kPa	[162.04; 471.20]	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			7.72409e+01
Coefficient B			-5.39795e+03
Coefficient C			-9.73971e+00
Coefficient D			1.15758e-05
Coefficient E			0.00000e+00
Temperature range, min.			162.04
Temperature range, max.			471.20
Pvap	4.88e-03	kPa	162.04	Calculated Property
Pvap	0.29	kPa	196.39	Calculated Property
Pvap	4.33	kPa	230.74	Calculated Property
Pvap	28.32	kPa	265.09	Calculated Property
Pvap	111.85	kPa	299.44	Calculated Property
Pvap	319.38	kPa	333.80	Calculated Property
Pvap	735.39	kPa	368.15	Calculated Property
Pvap	1464.61	kPa	402.50	Calculated Property
Pvap	2643.90	kPa	436.85	Calculated Property
Pvap	4467.78	kPa	471.20	Calculated Property
Pvap	[6.31; 88.57]	kPa	[236.48; 293.04]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38802e+01
Coefficient B			-2.42194e+03
Coefficient C			-3.52870e+01
Reference			Osborne, Garner, et al., 1941
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			236.48
Temperature range, max.			293.04
Pvap	6.31	kPa	236.48	Calculated Property
Pvap	9.09	kPa	242.76	Calculated Property
Pvap	12.81	kPa	249.05	Calculated Property
Pvap	17.70	kPa	255.33	Calculated Property
Pvap	24.03	kPa	261.62	Calculated Property
Pvap	32.08	kPa	267.90	Calculated Property
Pvap	42.19	kPa	274.19	Calculated Property
Pvap	54.71	kPa	280.47	Calculated Property
Pvap	70.03	kPa	286.76	Calculated Property
Pvap	88.57	kPa	293.04	Calculated Property
Pvap	[9.37; 323.52]	kPa	[243.50; 334.30]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38488e+01
Coefficient B			-2.40229e+03
Coefficient C			-3.66020e+01
Reference			Benning and McHarness, 1940
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			243.50
Temperature range, max.			334.30
Pvap	9.37	kPa	243.50	Calculated Property
Pvap	16.08	kPa	253.59	Calculated Property
Pvap	26.30	kPa	263.68	Calculated Property
Pvap	41.25	kPa	273.77	Calculated Property
Pvap	62.36	kPa	283.86	Calculated Property
Pvap	91.27	kPa	293.94	Calculated Property
Pvap	129.80	kPa	304.03	Calculated Property
Pvap	179.93	kPa	314.12	Calculated Property
Pvap	243.76	kPa	324.21	Calculated Property
Pvap	323.52	kPa	334.30	Calculated Property
Pvap	[9.37; 323.52]	kPa	[243.50; 334.30]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38488e+01
Coefficient B			-2.40229e+03
Coefficient C			-3.66020e+01
Reference			Benning and McHarness, 1940, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			243.50
Temperature range, max.			334.30
Pvap	9.37	kPa	243.50	Calculated Property
Pvap	16.08	kPa	253.59	Calculated Property
Pvap	26.30	kPa	263.68	Calculated Property
Pvap	41.25	kPa	273.77	Calculated Property
Pvap	62.36	kPa	283.86	Calculated Property
Pvap	91.27	kPa	293.94	Calculated Property
Pvap	129.80	kPa	304.03	Calculated Property
Pvap	179.93	kPa	314.12	Calculated Property
Pvap	243.76	kPa	324.21	Calculated Property
Pvap	323.52	kPa	334.30	Calculated Property

Similar Compounds

Find more compounds similar to Trichloromonofluoromethane.

Mixtures

• Trichloromonofluoromethane + Water
• Chlorotrifluoromethane + Trichloromonofluoromethane
• Dichlorodifluoromethane + Trichloromonofluoromethane
• Methane, chlorodifluoro- + Trichloromonofluoromethane

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Hydrogen substitution effect on the solubility of perhalogenated compounds in ionic liquid [bmim][PF6]
• Experimental P-T- and Enthalpy-Increment Measurements of an Equimolar Mixture of Trichlorofluoromethane (R-11) + Dichlorodifluoromethane (R-12)
• Experimental P-T- and Enthalpy-Increment Measurements of Trichlorofluoromethane, R-11 (x=0.83) + Chlorodifluoromethane, R-22 (1-x)
• Experimental P-T-rho and Enthalpy-Increment Measurements of an Equimolar Mixture of Trichlorofluoromethane (R-11) + Chlorotrifluoromethane (R-13)
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• 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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