Chemical Properties of Chlorine (CAS 7782-50-5)

InChI

InChI=1S/Cl2/c1-2

InChI Key

KZBUYRJDOAKODT-UHFFFAOYSA-N

Formula

Cl2

SMILES

ClCl

Molecular Weight¹

70.91

CAS

7782-50-5

Other Names

• Bertholite
• Chloor
• Chlor
• Chlore
• Chlorine mol.
• Chlorine molecule
• Cl2
• Cloro
• Diatomic chlorine
• Molecular chlorine
• UN 1017
• chlorine, diatomic

• 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).
• 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 a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_c : Critical density (kg/m³).
• ρ_g : Gas Density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• S°_{gas,1 bar} : Molar entropy at standard conditions (1 bar) (J/mol×K).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• V_COSTALD : COSTALD Characteristic Volume (m³/kmol).
• ω_SRK : SRK acentric factor.
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.0730; 0.0900]
ω	0.0730		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.0730		ChemSep v8.3 pure component data Compiled value
ω	0.0900		KDB
μ	[0.00; 0.00]	debye
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
μ	0.00	debye	KDB
EA	[1.02; 3.20]	eV
EA	2.50 ± 0.20	eV	NIST
EA	2.33	eV	NIST
EA	2.40 ± 0.20	eV	NIST
EA	2.32 ± 0.10	eV	NIST
EA	2.45 ± 0.15	eV	NIST
EA	2.46 ± 0.14	eV	NIST
EA	2.38 ± 0.10	eV	NIST
EA	2.52 ± 0.17	eV	NIST
EA	Outlier 1.02 ± 0.05	eV	NIST
EA	3.20 ± 0.20	eV	NIST
ΔfG°	0.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[0.00; 0.00]	kJ/mol
ΔfH°gas	0.00	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	0.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	4.15	kJ/mol	Joback Calculated Property
IE	[11.48; 11.59]	eV
IE	11.48 ± 0.00	eV	NIST
IE	11.48 ± 0.01	eV	NIST
IE	11.50	eV	NIST
IE	11.51 ± 0.01	eV	NIST
IE	11.48 ± 0.01	eV	NIST
IE	11.49	eV	NIST
IE	11.49	eV	NIST
IE	11.48 ± 0.01	eV	NIST
IE	11.49	eV	NIST
IE	Outlier 11.59	eV	NIST
logPoct/wat	1.379		Crippen Calculated Property
McVol	35.340	ml/mol	McGowan Calculated Property
NFPA Health	3		KDB
NFPA Safety	1		KDB
Pc	[7700.00; 7991.40]	kPa
Pc	7700.70	kPa	Mathews (1972), critical constants of inorganic substances Compiled value
Pc	7700.70	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	7700.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	7700.00	kPa	Air Liquide Gas Encyclopedia
Pc	7991.00	kPa	KDB
Pc	7991.40	kPa	NIST
Pc	7977.00 ± 50.00	kPa	NIST
Ptriple	[1.37; 1.39]	kPa
Ptriple	1.39	kPa	Staveley, Lobo and Calado (1981), triple points Compiled value
Ptriple	1.37	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	1.39	kPa	KDB
Ptriple	1.39 ± 0.00	kPa	NIST
ρc	576.78	kg/m3	NIST
S°gas,1 bar	223.08 ± 0.01	J/mol×K	NIST
Tboil	[239.05; 239.50]	K
Tboil	239.12	K	ChemSep v8.3 pure component data Compiled value
Tboil	239.05	K	Air Liquide Gas Encyclopedia
Tboil	239.11	K	KDB
Tboil	239.50 ± 0.60	K	NIST
Tc	[416.90; 417.15]	K
Tc	417.00	K	Mathews (1972), critical constants of inorganic substances Compiled value
Tc	417.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	417.00	K	ChemSep v8.3 pure component data Compiled value
Tc	Outlier 417.15	K	Air Liquide Gas Encyclopedia
Tc	416.90	K	KDB
Tc	416.96	K	NIST
Tc	416.90 ± 0.50	K	NIST
Tfus	[171.60; 172.15]	K
Tfus	172.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	172.12	K	ChemSep v8.3 pure component data Compiled value
Tfus	172.15	K	Air Liquide Gas Encyclopedia
Tfus	171.60	K	KDB
Ttriple	[172.12; 172.23]	K
Ttriple	172.23	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	172.12	K	ChemSep v8.3 pure component data Compiled value
Ttriple	172.17	K	KDB
Ttriple	172.17 ± 0.05	K	NIST
Ttriple	172.12 ± 0.15	K	NIST
UQi	1.52		ChemSep v8.3 pure component data Compiled value
URi	1.59		ChemSep v8.3 pure component data Compiled value
Vc	[0.123; 0.124]	m3/kmol
Vc	0.124	m3/kmol	Mathews (1972), critical constants of inorganic substances Compiled value
Vc	0.124	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.124	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.123	m3/kmol	KDB
VCOSTALD	0.12	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.08		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2750000; 0.2835550]
Zc	0.2750000		Mathews (1972), critical constants of inorganic substances Compiled value
Zc	0.2750000		ChemSep v8.3 pure component data Compiled value
Zc	0.2835550		KDB
Zra	[0.28; 0.28]
Zra	0.28		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.28		KDB

Cheméo can also estimate Enthalpy of vaporization at standard conditions, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
ΔfusH	6.41	kJ/mol	172.15	Air Liquide Gas Encyclopedia
ΔvapH	20.41	kJ/mol	239.05	Air Liquide Gas Encyclopedia
ρg	[3.04; 3.71]	kg/m3	[239.05; 288.15]
ρg	3.71	kg/m3	239.05	Air Liquide Gas Encyclopedia
ρg	3.04	kg/m3	288.15	Air Liquide Gas Encyclopedia
ρl	[1562.50; 1563.00]	kg/m3	[239.00; 239.05]
ρl	1563.00	kg/m3	239.00	KDB
ρl	1562.50	kg/m3	239.05	Air Liquide Gas Encyclopedia

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[28.97; 38.11]	J/mol×K	[50.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			2.89580e+01
Coefficient B			-3.98030e+02
Coefficient C			3.21724e+00
Coefficient D			-1.06810e-03
Coefficient E			3.84140e-07
Temperature range, min.			50.00
Temperature range, max.			1500.00
Cp,gas	28.97	J/mol×K	50.00	Calculated Property
Cp,gas	32.03	J/mol×K	211.11	Calculated Property
Cp,gas	35.03	J/mol×K	372.22	Calculated Property
Cp,gas	36.43	J/mol×K	533.33	Calculated Property
Cp,gas	37.02	J/mol×K	694.44	Calculated Property
Cp,gas	37.28	J/mol×K	855.56	Calculated Property
Cp,gas	37.43	J/mol×K	1016.67	Calculated Property
Cp,gas	37.58	J/mol×K	1177.78	Calculated Property
Cp,gas	37.79	J/mol×K	1338.89	Calculated Property
Cp,gas	38.11	J/mol×K	1500.00	Calculated Property
Cp,gas	[33.94; 37.44]	J/mol×K	[298.00; 1000.00]	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			3.30506e+01
Coefficient B			1.22294e+01
Coefficient C			-1.20651e+01
Coefficient D			4.38533e+00
Coefficient E			-1.59494e-01
Reference			Chase, 1998
Comment			F=-10.83480, G=259.0290, H=0.000000; Data last reviewed in June, 1982
Temperature range, min.			298.00
Temperature range, max.			1000.00
Cp,gas	33.94	J/mol×K	298.00	Calculated Property
Cp,gas	35.05	J/mol×K	376.00	Calculated Property
Cp,gas	35.75	J/mol×K	454.00	Calculated Property
Cp,gas	36.24	J/mol×K	532.00	Calculated Property
Cp,gas	36.59	J/mol×K	610.00	Calculated Property
Cp,gas	36.84	J/mol×K	688.00	Calculated Property
Cp,gas	37.04	J/mol×K	766.00	Calculated Property
Cp,gas	37.19	J/mol×K	844.00	Calculated Property
Cp,gas	37.32	J/mol×K	922.00	Calculated Property
Cp,gas	37.44	J/mol×K	1000.00	Calculated Property
Cp,gas	[37.31; 40.08]	J/mol×K	[1000.00; 3000.00]	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			4.26773e+01
Coefficient B			-5.00957e+00
Coefficient C			1.90462e+00
Coefficient D			-1.65641e-01
Coefficient E			-2.09848e+00
Reference			Chase, 1998
Comment			F=-17.28980, G=269.8400, H=0.000000; Data last reviewed in June, 1982
Temperature range, min.			1000.00
Temperature range, max.			3000.00
Cp,gas	37.31	J/mol×K	1000.00	Calculated Property
Cp,gas	37.69	J/mol×K	1222.22	Calculated Property
Cp,gas	37.91	J/mol×K	1444.44	Calculated Property
Cp,gas	38.10	J/mol×K	1666.67	Calculated Property
Cp,gas	38.31	J/mol×K	1888.89	Calculated Property
Cp,gas	38.56	J/mol×K	2111.11	Calculated Property
Cp,gas	38.87	J/mol×K	2333.33	Calculated Property
Cp,gas	39.23	J/mol×K	2555.56	Calculated Property
Cp,gas	39.64	J/mol×K	2777.78	Calculated Property
Cp,gas	40.08	J/mol×K	3000.00	Calculated Property
Cp,gas	[40.07; 37.58]	J/mol×K	[3000.00; 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			-4.25535e+01
Coefficient B			4.16857e+01
Coefficient C			-7.12683e+00
Coefficient D			3.87839e-01
Coefficient E			1.01144e+02
Reference			Chase, 1998
Comment			F=132.7640, G=264.7860, H=0.000000; Data last reviewed in June, 1982
Temperature range, min.			3000.00
Temperature range, max.			6000.00
Cp,gas	40.07	J/mol×K	3000.00	Calculated Property
Cp,gas	40.68	J/mol×K	3333.33	Calculated Property
Cp,gas	41.12	J/mol×K	3666.67	Calculated Property
Cp,gas	41.30	J/mol×K	4000.00	Calculated Property
Cp,gas	41.20	J/mol×K	4333.33	Calculated Property
Cp,gas	40.83	J/mol×K	4666.67	Calculated Property
Cp,gas	40.23	J/mol×K	5000.00	Calculated Property
Cp,gas	39.44	J/mol×K	5333.33	Calculated Property
Cp,gas	38.54	J/mol×K	5666.67	Calculated Property
Cp,gas	37.58	J/mol×K	6000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[66.55; 66.55]	J/mol×K	[172.12; 239.12]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			6.65470e+01
Coefficient B			1.24880e+04
Coefficient C			-2.53208e+02
Coefficient D			-2.72660e+00
Coefficient E			-2.15180e-02
Temperature range, min.			172.12
Temperature range, max.			239.12
Cp,liquid	66.55	J/mol×K	172.12	Calculated Property
Cp,liquid	66.55	J/mol×K	179.56	Calculated Property
Cp,liquid	66.55	J/mol×K	187.01	Calculated Property
Cp,liquid	66.55	J/mol×K	194.45	Calculated Property
Cp,liquid	66.55	J/mol×K	201.90	Calculated Property
Cp,liquid	66.55	J/mol×K	209.34	Calculated Property
Cp,liquid	66.55	J/mol×K	216.79	Calculated Property
Cp,liquid	66.55	J/mol×K	224.23	Calculated Property
Cp,liquid	66.55	J/mol×K	231.68	Calculated Property
Cp,liquid	66.55	J/mol×K	239.12	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0010193; 0.0002806]	Pa×s	[172.12; 333.72]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.13510e+01
Coefficient B			5.02600e+02
Coefficient C			3.05060e-01
Coefficient D			-9.52370e-07
Coefficient E			2.00000e+00
Temperature range, min.			172.12
Temperature range, max.			333.72
η	0.0010193	Pa×s	172.12	Calculated Property
η	0.0007924	Pa×s	190.08	Calculated Property
η	0.0006439	Pa×s	208.03	Calculated Property
η	0.0005410	Pa×s	225.99	Calculated Property
η	0.0004664	Pa×s	243.94	Calculated Property
η	0.0004103	Pa×s	261.90	Calculated Property
η	0.0003667	Pa×s	279.85	Calculated Property
η	0.0003321	Pa×s	297.81	Calculated Property
η	0.0003040	Pa×s	315.76	Calculated Property
η	0.0002806	Pa×s	333.72	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[22.83; 1.68]	kJ/mol	[172.12; 416.75]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			2.96010e+01
Coefficient B			7.73340e-01
Coefficient C			-1.02790e+00
Coefficient D			9.33680e-01
Coefficient E			-2.92600e-01
Critical temperature, Tc (K)			4.17000e+02
Temperature range, min.			172.12
Temperature range, max.			416.75
ΔvapH	22.83	kJ/mol	172.12	Calculated Property
ΔvapH	21.90	kJ/mol	199.30	Calculated Property
ΔvapH	20.91	kJ/mol	226.48	Calculated Property
ΔvapH	19.82	kJ/mol	253.66	Calculated Property
ΔvapH	18.60	kJ/mol	280.84	Calculated Property
ΔvapH	17.18	kJ/mol	308.03	Calculated Property
ΔvapH	15.47	kJ/mol	335.21	Calculated Property
ΔvapH	13.31	kJ/mol	362.39	Calculated Property
ΔvapH	10.26	kJ/mol	389.57	Calculated Property
ΔvapH	1.68	kJ/mol	416.75	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.37; 7789.75]	kPa	[172.12; 417.15]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42483e+01
Coefficient B			-2.08776e+03
Coefficient C			-2.23200e+01
Temperature range, min.			172.12
Temperature range, max.			417.15
Pvap	1.37	kPa	172.12	Calculated Property
Pvap	11.64	kPa	199.35	Calculated Property
Pvap	56.08	kPa	226.57	Calculated Property
Pvap	186.61	kPa	253.80	Calculated Property
Pvap	482.11	kPa	281.02	Calculated Property
Pvap	1039.61	kPa	308.25	Calculated Property
Pvap	1961.40	kPa	335.47	Calculated Property
Pvap	3343.16	kPa	362.70	Calculated Property
Pvap	5265.56	kPa	389.92	Calculated Property
Pvap	7789.75	kPa	417.15	Calculated Property
Pvap	[1.08; 7786.61]	kPa	[169.02; 417.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			3.88682e+01
Coefficient B			-3.29270e+03
Coefficient C			-3.79260e+00
Coefficient D			4.98630e-06
Coefficient E			2.00000e+00
Temperature range, min.			169.02
Temperature range, max.			417.15
Pvap	1.08	kPa	169.02	Calculated Property
Pvap	9.80	kPa	196.59	Calculated Property
Pvap	49.54	kPa	224.16	Calculated Property
Pvap	170.22	kPa	251.73	Calculated Property
Pvap	449.03	kPa	279.30	Calculated Property
Pvap	982.22	kPa	306.87	Calculated Property
Pvap	1874.74	kPa	334.44	Calculated Property
Pvap	3233.58	kPa	362.01	Calculated Property
Pvap	5166.67	kPa	389.58	Calculated Property
Pvap	7786.61	kPa	417.15	Calculated Property
Pvap	[0.14; 96.65]	kPa	[155.00; 239.40]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.15620e+01
Coefficient B			-1.22173e+03
Coefficient C			-6.46390e+01
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			155.00
Temperature range, max.			239.40
Pvap	0.14	kPa	155.00	Calculated Property
Pvap	0.50	kPa	164.38	Calculated Property
Pvap	1.44	kPa	173.76	Calculated Property
Pvap	3.50	kPa	183.13	Calculated Property
Pvap	7.45	kPa	192.51	Calculated Property
Pvap	14.30	kPa	201.89	Calculated Property
Pvap	25.27	kPa	211.27	Calculated Property
Pvap	41.71	kPa	220.64	Calculated Property
Pvap	65.02	kPa	230.02	Calculated Property
Pvap	96.65	kPa	239.40	Calculated Property
Pvap	[101.78; 6095.27]	kPa	[239.40; 400.30]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.44790e+01
Coefficient B			-2.23349e+03
Coefficient C			-1.27910e+01
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			239.40
Temperature range, max.			400.30
Pvap	101.78	kPa	239.40	Calculated Property
Pvap	209.26	kPa	257.28	Calculated Property
Pvap	389.96	kPa	275.16	Calculated Property
Pvap	671.24	kPa	293.03	Calculated Property
Pvap	1082.54	kPa	310.91	Calculated Property
Pvap	1653.96	kPa	328.79	Calculated Property
Pvap	2414.85	kPa	346.67	Calculated Property
Pvap	3392.73	kPa	364.54	Calculated Property
Pvap	4612.37	kPa	382.42	Calculated Property
Pvap	6095.27	kPa	400.30	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1726.68; 562.33]	kg/m3	[172.12; 417.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			1.29708e+02
Coefficient B			2.50000e-01
Coefficient C			4.17160e+02
Coefficient D			2.67530e-01
Temperature range, min.			172.12
Temperature range, max.			417.15
ρl	1726.68	kg/m3	172.12	Calculated Property
ρl	1663.47	kg/m3	199.35	Calculated Property
ρl	1596.83	kg/m3	226.57	Calculated Property
ρl	1525.93	kg/m3	253.80	Calculated Property
ρl	1449.55	kg/m3	281.02	Calculated Property
ρl	1365.77	kg/m3	308.25	Calculated Property
ρl	1271.28	kg/m3	335.47	Calculated Property
ρl	1159.41	kg/m3	362.70	Calculated Property
ρl	1011.92	kg/m3	389.92	Calculated Property
ρl	562.33	kg/m3	417.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.00]	N/m	[172.12; 404.25]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-8.28030e-02
Coefficient B			-1.88900e+00
Coefficient C			-1.85850e+00
Coefficient D			-1.34220e-03
Coefficient E			-4.13940e-07
Temperature range, min.			172.12
Temperature range, max.			404.25
γ	0.04	N/m	172.12	Calculated Property
γ	0.03	N/m	197.91	Calculated Property
γ	0.03	N/m	223.70	Calculated Property
γ	0.03	N/m	249.50	Calculated Property
γ	0.02	N/m	275.29	Calculated Property
γ	0.02	N/m	301.08	Calculated Property
γ	0.01	N/m	326.87	Calculated Property
γ	0.01	N/m	352.67	Calculated Property
γ	0.01	N/m	378.46	Calculated Property
γ	0.00	N/m	404.25	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.03]	W/m×K	[172.12; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			9.65880e-04
Coefficient B			5.49950e-01
Coefficient C			4.34260e+02
Coefficient D			3.60590e+03
Temperature range, min.			172.12
Temperature range, max.			1000.00
λgas	0.00	W/m×K	172.12	Calculated Property
λgas	0.01	W/m×K	264.11	Calculated Property
λgas	0.01	W/m×K	356.09	Calculated Property
λgas	0.01	W/m×K	448.08	Calculated Property
λgas	0.02	W/m×K	540.07	Calculated Property
λgas	0.02	W/m×K	632.05	Calculated Property
λgas	0.02	W/m×K	724.04	Calculated Property
λgas	0.03	W/m×K	816.03	Calculated Property
λgas	0.03	W/m×K	908.01	Calculated Property
λgas	0.03	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.19; 0.07]	W/m×K	[170.00; 410.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			-4.87430e-01
Coefficient B			1.32290e+01
Coefficient C			-4.93710e-01
Coefficient D			5.29890e-04
Coefficient E			-2.04910e-06
Temperature range, min.			170.00
Temperature range, max.			410.00
λliquid	0.19	W/m×K	170.00	Calculated Property
λliquid	0.18	W/m×K	196.67	Calculated Property
λliquid	0.17	W/m×K	223.33	Calculated Property
λliquid	0.16	W/m×K	250.00	Calculated Property
λliquid	0.15	W/m×K	276.67	Calculated Property
λliquid	0.13	W/m×K	303.33	Calculated Property
λliquid	0.12	W/m×K	330.00	Calculated Property
λliquid	0.10	W/m×K	356.67	Calculated Property
λliquid	0.09	W/m×K	383.33	Calculated Property
λliquid	0.07	W/m×K	410.00	Calculated Property

Similar Compounds

Find more compounds similar to Chlorine.

Sources

• Air Liquide Gas Encyclopedia
• Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
• Mathews (1972), critical constants of inorganic substances ChEDL chemicals 1.5.2, from Mathews, J. F. Critical Constants of Inorganic Substances. Chem. Rev. 1972, 72, 71-100.
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Crippen Method
• Low-Temperature Heat Capacities and Standard Molar Enthalpy of Formation of Dichloro Bis(2-aminopyridine) Zinc (II), ZnCl2(C5H6N2)2(s)
• Standard molar enthalpies of formation of hydroxy-, chlor-, and bromapatite
• Thermochemical study of some dichloroacetophenone isomers
• Experimental and computational thermochemical studies of benzoxazole and two chlorobenzoxadole derivatives
• Thermochemistry on crystalline compounds bis-(n-dodecylammonium) tetrachlorometallates (n-C12H25NH3)2MCl4(s) (M = Cu and Cd)
• Phase equilibria of the systems of CsCl + ErCl3 + H2O and CsCl + ErCl3 + HCl (~10.7%, ~14.4%) + H2O at T = 298.15 K and the standard molar enthalpies of formation of solid phase compounds
• Thermodynamic study on complex of neodymium with glycine
• Isomorphism and phase diagram of Pb5(PO4)3F-Pb5(PO4)3Cl system
• Low-Temperature Heat Capacities and Standard Molar Enthalpy of Formation of Ethylenediammonium Tetrachlorocobaltate(II) Chloride (H3NCH2CH2NH3)2[CoCl4]Cl2(s)
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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