Formic acid, propyl ester (CAS 110-74-7)

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Physical Properties

Property	Value	Unit	Source
ω	0.3140		KDB
PAff	804.90	kJ/mol	NIST
BasG	773.90	kJ/mol	NIST
Δ_cH°_solid	-2217.00 ± 42.00	kJ/mol	NIST
μ	1.90	debye	KDB
Δ_fG°	-221.72	kJ/mol	Joback Calculated Property
Δ_fH°_gas	-343.69	kJ/mol	Joback Calculated Property
Δ_fH°_solid	-500.00 ± 42.00	kJ/mol	NIST
Δ_fusH°	9.59	kJ/mol	Joback Calculated Property
Δ_vapH°	[32.50; 37.61]	kJ/mol
Δ_vapH°	37.61	kJ/mol	NIST
Δ_vapH°	37.50 ± 0.10	kJ/mol	NIST
Δ_vapH°	32.50 ± 0.04	kJ/mol	NIST
IE	[10.30; 10.62]	eV
IE	10.54 ± 0.05	eV	NIST
IE	Outlier 10.30 ± 0.20	eV	NIST
IE	10.50 ± 0.05	eV	NIST
IE	10.50	eV	NIST
IE	10.62	eV	NIST
IE	10.54 ± 0.01	eV	NIST
log₁₀WS	[-0.49; -0.49]
log₁₀WS	-0.49		Aq. Sol...
log₁₀WS	-0.49		Estimat...
logP_oct/wat	0.569		Crippen Calculated Property
McVol	74.660	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
P_c	[4060.00; 4330.00]	kPa
P_c	4060.00	kPa	KDB
P_c	4061.00 ± 60.79	kPa	NIST
P_c	4061.00 ± 40.00	kPa	NIST
P_c	4330.00 ± 303.98	kPa	NIST
ρ_c	[304.84; 309.51]	kg/m³
ρ_c	309.34 ± 5.29	kg/m³	NIST
ρ_c	309.51 ± 4.41	kg/m³	NIST
ρ_c	304.84 ± 5.29	kg/m³	NIST
I_np	[559.00; 606.00]
I_np	564.00		NIST
I_np	572.00		NIST
I_np	576.00		NIST
I_np	570.00		NIST
I_np	602.00		NIST
I_np	559.00		NIST
I_np	592.00		NIST
I_np	574.00		NIST
I_np	570.00		NIST
I_np	602.00		NIST
I_np	604.00		NIST
I_np	605.00		NIST
I_np	604.00		NIST
I_np	602.00		NIST
I_np	602.00		NIST
I_np	606.00		NIST
I_np	602.00		NIST
I_np	606.00		NIST
I_np	606.00		NIST
I_np	603.00		NIST
I_np	603.00		NIST
I_np	602.00		NIST
I_np	564.00		NIST
I_np	559.00		NIST
I	[892.00; 916.00]
I	892.00		NIST
I	907.00		NIST
I	916.00		NIST
I	892.00		NIST
T_boil	[353.92; 354.50]	K
T_boil	354.00	K	KDB
T_boil	353.92	K	Solutio...
T_boil	353.92	K	Isobari...
T_boil	Outlier 354.50	K	NIST
T_boil	354.00	K	NIST
T_boil	354.05 ± 0.20	K	NIST
T_boil	354.00 ± 0.10	K	NIST
T_boil	354.15 ± 2.00	K	NIST
T_boil	354.00 ± 0.50	K	NIST
T_boil	354.00 ± 0.50	K	NIST
T_boil	354.10 ± 0.40	K	NIST
T_boil	353.95 ± 1.00	K	NIST
T_boil	354.10 ± 1.00	K	NIST
T_boil	354.40 ± 0.30	K	NIST
T_boil	354.05 ± 0.50	K	NIST
T_boil	354.00 ± 1.00	K	NIST
T_boil	354.05 ± 0.50	K	NIST
T_boil	354.40 ± 0.70	K	NIST
T_boil	354.00 ± 2.00	K	NIST
T_boil	354.15 ± 2.00	K	NIST
T_c	[533.70; 538.00]	K
T_c	538.00	K	KDB
T_c	538.00	K	NIST
T_c	538.00 ± 1.00	K	NIST
T_c	538.00 ± 1.00	K	NIST
T_c	533.70 ± 4.00	K	NIST
T_c	534.00 ± 4.00	K	NIST
T_fus	[180.20; 180.30]	K
T_fus	180.20	K	Aq. Sol...
T_fus	180.20	K	KDB
T_fus	180.30 ± 0.40	K	NIST
V_c	0.285	m³/kmol	KDB
Z_c	0.2586740		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[132.08; 169.38]	J/mol×K	[362.00; 535.90]

C_p,gas	132.08	J/mol×K	362.00	Joback Calculated Property
C_p,gas	138.73	J/mol×K	390.98	Joback Calculated Property
C_p,gas	145.20	J/mol×K	419.97	Joback Calculated Property
C_p,gas	151.51	J/mol×K	448.95	Joback Calculated Property
C_p,gas	157.65	J/mol×K	477.93	Joback Calculated Property
C_p,gas	163.60	J/mol×K	506.91	Joback Calculated Property
C_p,gas	169.38	J/mol×K	535.90	Joback Calculated Property
C_p,liquid	[171.42; 172.10]	J/mol×K	[298.15; 298.15]
C_p,liquid	172.10	J/mol×K	298.15	NIST
C_p,liquid	171.42	J/mol×K	298.15	NIST
C_p,liquid	172.07	J/mol×K	298.15	NIST
η	[0.0004310; 0.0004770]	Pa×s	[303.15; 313.15]
η	0.0004770	Pa×s	303.15	Density...
η	0.0004560	Pa×s	308.15	Density...
η	0.0004310	Pa×s	313.15	Density...
Δ_vapH	[32.70; 36.80]	kJ/mol	[292.50; 436.00]

Δ_vapH	36.80	kJ/mol	292.50	NIST
Δ_vapH	36.50 ± 0.10	kJ/mol	313.00	NIST
Δ_vapH	35.80 ± 0.10	kJ/mol	326.00	NIST
Δ_vapH	35.60	kJ/mol	327.00	NIST
Δ_vapH	35.30	kJ/mol	327.50	NIST
Δ_vapH	35.40 ± 0.10	kJ/mol	331.00	NIST
Δ_vapH	34.40 ± 0.10	kJ/mol	344.00	NIST
Δ_vapH	33.80 ± 0.10	kJ/mol	351.00	NIST
Δ_vapH	33.61	kJ/mol	354.00	NIST
Δ_vapH	33.50 ± 0.10	kJ/mol	355.00	NIST
Δ_vapH	32.90 ± 0.10	kJ/mol	363.00	NIST
Δ_vapH	32.70	kJ/mol	436.00	NIST
P_vap	101.32	kPa	353.92	Isobari...
n₀	[1.37180; 1.37260]		[303.15; 303.15]
n₀	1.37180		303.15	Correla...
n₀	1.37260		303.15	Excess ...
ρ_l	[899.81; 911.00]	kg/m³	[289.00; 298.15]
ρ_l	911.00	kg/m³	289.00	KDB
ρ_l	907.97	kg/m³	291.15	Experim...
ρ_l	899.86	kg/m³	298.15	Experim...
ρ_l	899.81	kg/m³	298.15	Thermod...

Correlations

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 202.63]	kPa	[263.26; 376.94]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.41082e+01
Coefficient B			-2.75112e+03
Coefficient C			-6.42010e+01
Temperature range, min.			263.26
Temperature range, max.			376.94

P_vap	1.33	kPa	263.26	Calculated Property
P_vap	3.04	kPa	275.89	Calculated Property
P_vap	6.32	kPa	288.52	Calculated Property
P_vap	12.16	kPa	301.15	Calculated Property
P_vap	21.88	kPa	313.78	Calculated Property
P_vap	37.20	kPa	326.42	Calculated Property
P_vap	60.25	kPa	339.05	Calculated Property
P_vap	93.54	kPa	351.68	Calculated Property
P_vap	139.93	kPa	364.31	Calculated Property
P_vap	202.63	kPa	376.94	Calculated Property
P_vap	[4.09e-04; 4001.42]	kPa	[180.25; 538.00]	KDB Vap...
Equation			ln(Pvp) = A + B/T + Cln(T) + DT^2
Coefficient A			6.34798e+01
Coefficient B			-6.18307e+03
Coefficient C			-7.14597e+00
Coefficient D			4.28442e-06
Temperature range, min.			180.25
Temperature range, max.			538.00

P_vap	4.09e-04	kPa	180.25	Calculated Property
P_vap	0.05	kPa	220.00	Calculated Property
P_vap	1.27	kPa	259.75	Calculated Property
P_vap	11.85	kPa	299.50	Calculated Property
P_vap	60.92	kPa	339.25	Calculated Property
P_vap	210.96	kPa	379.00	Calculated Property
P_vap	557.47	kPa	418.75	Calculated Property
P_vap	1217.89	kPa	458.50	Calculated Property
P_vap	2320.52	kPa	498.25	Calculated Property
P_vap	4001.42	kPa	538.00	Calculated Property

Similar Compounds

Find more compounds similar to Formic acid, propyl ester.

Mixtures

Sources

KDB Vapor Pressure Data
Crippen Method
Excess properties and isobaric vapor liquid equilibria for four binary systems of alkyl (methyl to butyl) methanoates with decane
Experimentation and thermodynamic representations of binaries containing compounds of low boiling points: Pentane and alkylmethanoates
Solutions of alkyl methanoates and alkanes: Simultaneous modeling of phase equilibria and mixing properties. Estimation of behavior by UNIFAC with recalculation of parameters
Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) V. Hex and Vex for 25 binary mixtures {xCu-1H2u-1CO2CH3 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) VII. HE m and VE m for 20 binary mixtures {xCu 1H2u 1CO2C3H7 + (1 x)a,x-ClCH2(CH2)v 2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6. An analysis of behavior using the COSMO-RS methodology
Correlation and Prediction of Excess Quantities and Vapor-Liquid Equilibria of Alkyl Esters + tert-Butyl Alcohol: Experimental Data for Propyl Esters + tert-Butyl Alcohol
Isobaric Vapor-Liquid Equilibrium Data and Excess Properties of Binary Systems Comprised of Alkyl Methanoates + Hexane
Excess Volumes of Binary Solutions of Methyl Formate, Ethyl Formate, Propyl Formate, and Benzyl Acetate with Bromo-, Chloro-, and Nitrobenzenes at (303.15, 308.15, and 313.15) K
Density and Viscosity of Propyl Formate + Aromatic Hydrocarbons at T = (303.15, 308.15, and 313.15) K
Joback Method
KDB
Aqueous Solubility Prediction Method
Estimated Solubility Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure

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Chemical Properties of Formic acid, propyl ester (CAS 110-74-7)