Chemical Properties of Butanoic acid, butyl ester (CAS 109-21-7)

InChI

InChI=1S/C8H16O2/c1-3-5-7-10-8(9)6-4-2/h3-7H2,1-2H3

InChI Key

XUPYJHCZDLZNFP-UHFFFAOYSA-N

Formula

C8H16O2

SMILES

CCCCOC(=O)CCC

Molecular Weight¹

144.21

CAS

109-21-7

Other Names

• 1-Butyl butyrate
• BUTYL ESTER BUTANOIC ACID
• Butyl butylate
• Butyl ester of butanoic acid
• Butyl n-butyrate
• Butyric acid, butyl ester
• NSC 8458
• butyl butanoate
• butyl butyrate
• n-Butyl butanoate
• n-Butyl n-butanoate
• n-Butyl n-butyrate
• n-Butyric acid n-butyl ester
• n-butyl butyrate

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• 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).
• 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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• 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).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.5422		Relay (1.0) Calculated Property
ΔcH°liquid	-4844.20	kJ/mol	NIST
Tflash,cc	326.15	K	NCMS SOLV-DB
ΔfG°	-293.89	kJ/mol	Joback Calculated Property
ΔfH°gas	-529.39	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	20.85	kJ/mol	Joback Calculated Property
ΔvapH°	50.34	kJ/mol	Relay (1.0) Calculated Property
IE	9.78	eV	Relay (1.0) Calculated Property
log10WS	-2.09		Relay (1.0) Calculated Property
logPoct/wat	2.060		NCMS SOLV-DB
McVol	131.020	ml/mol	McGowan Calculated Property
NFPA Fire	2		NCMS SOLV-DB
NFPA Health	2		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	2548.19	kPa	Joback Calculated Property
Inp	[940.00; 1009.00]
Inp	979.40		NIST
Inp	991.00		NIST
Inp	982.00		NIST
Inp	985.00		NIST
Inp	978.00		NIST
Inp	978.00		NIST
Inp	Outlier 940.00		NIST
Inp	969.00		NIST
Inp	977.00		NIST
Inp	980.00		NIST
Inp	985.00		NIST
Inp	980.00		NIST
Inp	983.00		NIST
Inp	977.00		NIST
Inp	982.00		NIST
Inp	990.00		NIST
Inp	982.00		NIST
Inp	982.00		NIST
Inp	978.00		NIST
Inp	983.00		NIST
Inp	985.00		NIST
Inp	996.00		NIST
Inp	969.00		NIST
Inp	996.00		NIST
Inp	993.00		NIST
Inp	993.00		NIST
Inp	998.00		NIST
Inp	994.00		NIST
Inp	1002.00		NIST
Inp	969.00		NIST
Inp	999.00		NIST
Inp	978.00		NIST
Inp	982.00		NIST
Inp	975.00		NIST
Inp	977.00		NIST
Inp	1001.00		NIST
Inp	998.00		NIST
Inp	990.00		NIST
Inp	994.00		NIST
Inp	994.00		NIST
Inp	996.00		NIST
Inp	985.00		NIST
Inp	970.00		NIST
Inp	1002.00		NIST
Inp	992.00		NIST
Inp	986.00		NIST
Inp	996.00		NIST
Inp	997.00		NIST
Inp	995.00		NIST
Inp	979.00		NIST
Inp	997.00		NIST
Inp	Outlier 1009.00		NIST
Inp	975.00		NIST
Inp	977.00		NIST
Inp	975.00		NIST
Inp	975.00		NIST
Inp	975.00		NIST
Inp	975.00		NIST
Inp	975.00		NIST
Inp	977.00		NIST
Inp	978.00		NIST
Inp	979.00		NIST
Inp	979.00		NIST
Inp	977.00		NIST
Inp	977.00		NIST
Inp	987.00		NIST
Inp	966.00		NIST
Inp	994.00		NIST
Inp	995.00		NIST
Inp	1000.00		NIST
Inp	994.00		NIST
Inp	996.00		NIST
Inp	979.00		NIST
Inp	981.00		NIST
Inp	969.00		NIST
Inp	993.00		NIST
Inp	996.00		NIST
Inp	993.00		NIST
Inp	993.00		NIST
Inp	999.00		NIST
Inp	993.00		NIST
Inp	1004.00		NIST
Inp	977.00		NIST
Inp	979.00		NIST
Inp	979.00		NIST
Inp	996.00		NIST
Inp	1002.00		NIST
Inp	975.00		NIST
Inp	979.40		NIST
Inp	978.00		NIST
Inp	985.00		NIST
I	[1183.00; 1251.00]
I	1215.00		NIST
I	1230.00		NIST
I	Outlier 1251.00		NIST
I	1221.00		NIST
I	1221.00		NIST
I	Outlier 1245.00		NIST
I	1232.00		NIST
I	1213.00		NIST
I	Outlier 1196.00		NIST
I	1224.00		NIST
I	1207.00		NIST
I	1212.00		NIST
I	1215.00		NIST
I	1201.00		NIST
I	1223.00		NIST
I	1218.00		NIST
I	1231.00		NIST
I	1220.00		NIST
I	1214.00		NIST
I	1240.00		NIST
I	Outlier 1183.00		NIST
I	1210.00		NIST
I	1218.00		NIST
I	1218.00		NIST
I	1219.00		NIST
I	1207.00		NIST
I	1221.00		NIST
I	1205.00		NIST
I	1216.00		NIST
I	1243.00		NIST
I	1226.00		NIST
I	1216.00		NIST
I	1207.00		NIST
I	1219.00		NIST
I	1208.00		NIST
I	1221.00		NIST
I	1218.00		NIST
I	1206.00		NIST
I	1206.00		NIST
I	1225.00		NIST
I	1228.00		NIST
I	1228.00		NIST
I	1220.00		NIST
I	1228.00		NIST
I	1228.00		NIST
I	1229.00		NIST
I	1229.00		NIST
I	1229.00		NIST
I	1216.00		NIST
I	1227.00		NIST
I	1223.00		NIST
I	1240.00		NIST
I	1208.00		NIST
I	1225.00		NIST
I	1228.00		NIST
I	1227.00		NIST
I	1215.00		NIST
Tboil	[436.75; 439.75]	K
Tboil	438.28	K	Measurement and Correlation of Vapor-Liquid Equilibrium for Binary Systems of Dimethyl Carbonate with Butyl Butyrate, o-Xylene, and Cyclohexanone at 101.3 kPa
Tboil	438.09	K	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Tboil	437.15	K	NCMS SOLV-DB
Tboil	437.70	K	NIST
Tboil	437.00	K	NIST
Tboil	438.15 ± 2.00	K	NIST
Tboil	439.55 ± 1.00	K	NIST
Tboil	439.65 ± 1.00	K	NIST
Tboil	437.65 ± 1.00	K	NIST
Tboil	439.15 ± 1.00	K	NIST
Tboil	439.55 ± 0.30	K	NIST
Tboil	438.00 ± 2.00	K	NIST
Tboil	437.15 ± 1.00	K	NIST
Tboil	439.40 ± 1.00	K	NIST
Tboil	436.75 ± 1.00	K	NIST
Tboil	439.75 ± 1.00	K	NIST
Tboil	439.60 ± 0.40	K	NIST
Tboil	438.90 ± 1.50	K	NIST
Tc	612.10 ± 0.60	K	NIST
Tfus	186.57	K	Relay (1.0) Calculated Property
Ttriple	[181.58; 181.68]	K
Ttriple	181.58 ± 0.10	K	NIST
Ttriple	181.68 ± 0.04	K	NIST
Vc	0.513	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
η	[0.0004860; 0.0009480]	Pa×s	[293.15; 343.15]
η	0.0009480	Pa×s	293.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0008760	Pa×s	298.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0008120	Pa×s	303.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0007550	Pa×s	308.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0007050	Pa×s	313.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0006590	Pa×s	318.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0006180	Pa×s	323.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0005810	Pa×s	328.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0005480	Pa×s	333.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0005170	Pa×s	338.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0004860	Pa×s	343.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
ΔfusH	[14.93; 14.93]	kJ/mol	[181.68; 181.70]
ΔfusH	14.93	kJ/mol	181.68	NIST
ΔfusH	14.93	kJ/mol	181.70	NIST
Pvap	[0.24; 164.01]	kPa	[298.15; 457.47]
Pvap	0.24	kPa	298.15	NCMS SOLV-DB
Pvap	40.28	kPa	405.54	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	41.53	kPa	406.59	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	42.86	kPa	407.56	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	44.16	kPa	408.56	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	45.06	kPa	409.28	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	46.65	kPa	410.43	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	48.06	kPa	411.38	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	49.58	kPa	412.43	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	50.53	kPa	413.11	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	52.27	kPa	414.21	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	53.34	kPa	414.92	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	54.86	kPa	415.87	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	56.21	kPa	416.72	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	57.51	kPa	417.51	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	58.78	kPa	418.27	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	60.01	kPa	418.98	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	61.31	kPa	419.74	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	62.83	kPa	420.59	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	64.02	kPa	421.26	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	65.51	kPa	422.07	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	66.81	kPa	422.76	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	67.91	kPa	423.35	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	69.74	kPa	424.29	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	70.42	kPa	424.66	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	72.31	kPa	425.59	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	73.25	kPa	426.07	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	74.67	kPa	426.78	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	76.02	kPa	427.43	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	77.34	kPa	428.05	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	78.82	kPa	428.69	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	79.99	kPa	429.28	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	81.71	kPa	430.02	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	82.77	kPa	430.48	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	84.03	kPa	431.04	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	85.54	kPa	431.70	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	86.67	kPa	432.27	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	87.95	kPa	432.82	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	89.55	kPa	433.42	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	90.72	kPa	433.90	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	91.87	kPa	434.46	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	93.35	kPa	435.06	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	94.70	kPa	435.61	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	96.15	kPa	436.09	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	97.30	kPa	436.56	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	98.75	kPa	437.11	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	100.18	kPa	437.66	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	101.32	kPa	438.09	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	101.30	kPa	438.28	Measurement and Correlation of Vapor-Liquid Equilibrium for Binary Systems of Dimethyl Carbonate with Butyl Butyrate, o-Xylene, and Cyclohexanone at 101.3 kPa
Pvap	102.63	kPa	438.67	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	104.00	kPa	439.18	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	105.50	kPa	439.66	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	106.67	kPa	440.16	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	108.31	kPa	440.68	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	109.48	kPa	441.11	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	110.68	kPa	441.60	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	112.07	kPa	442.01	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	113.34	kPa	442.53	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	114.71	kPa	442.93	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	116.00	kPa	443.44	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	117.43	kPa	443.86	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	118.65	kPa	444.34	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	120.03	kPa	444.78	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	121.28	kPa	445.21	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	122.76	kPa	445.62	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	124.03	kPa	446.04	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	125.37	kPa	446.47	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	126.64	kPa	446.87	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	128.00	kPa	447.33	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	129.33	kPa	447.74	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	130.73	kPa	448.18	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	132.01	kPa	448.54	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	133.41	kPa	448.97	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	134.68	kPa	449.36	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	135.99	kPa	449.75	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	137.35	kPa	450.15	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	138.69	kPa	450.55	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	140.07	kPa	450.94	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	141.21	kPa	451.29	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	142.69	kPa	451.71	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	143.97	kPa	452.07	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	145.69	kPa	452.55	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	146.84	kPa	452.88	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	148.17	kPa	453.25	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	149.33	kPa	453.58	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	150.73	kPa	453.95	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	152.16	kPa	454.34	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	153.29	kPa	454.65	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	154.65	kPa	455.02	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	155.97	kPa	455.37	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	157.25	kPa	455.71	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	158.69	kPa	456.09	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	159.94	kPa	456.42	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	161.37	kPa	456.79	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	162.68	kPa	457.13	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Pvap	164.01	kPa	457.47	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
n0	[1.40400; 1.40600]		[298.15; 298.15]
n0	1.40400		298.15	Thermodynamic study of (alkyl esters + a,x-alkyl dihalides)III. HE m and V E m for 20 binary mixtures {xCu-1H2u-1CO2C4H9 + (1 - x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6
n0	1.40600		298.15	NCMS SOLV-DB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[191.53; 440.16]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			2.10250e+01
Coefficient B			7.09040e-01
Coefficient C			-3.16800e-04
Coefficient D			2.69000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	191.53	J/mol×K	273.00	Calculated Property
Cp,gas	233.41	J/mol×K	353.78	Calculated Property
Cp,gas	271.53	J/mol×K	434.56	Calculated Property
Cp,gas	305.97	J/mol×K	515.33	Calculated Property
Cp,gas	336.82	J/mol×K	596.11	Calculated Property
Cp,gas	364.16	J/mol×K	676.89	Calculated Property
Cp,gas	388.08	J/mol×K	757.67	Calculated Property
Cp,gas	408.66	J/mol×K	838.44	Calculated Property
Cp,gas	426.00	J/mol×K	919.22	Calculated Property
Cp,gas	440.16	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[327.52; 466.20]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.48960e+01
Coefficient B			-3.86487e+03
Coefficient C			-6.29560e+01
Temperature range, min.			327.52
Temperature range, max.			466.20
Pvap	1.33	kPa	327.52	Calculated Property
Pvap	2.98	kPa	342.93	Calculated Property
Pvap	6.12	kPa	358.34	Calculated Property
Pvap	11.71	kPa	373.75	Calculated Property
Pvap	21.07	kPa	389.16	Calculated Property
Pvap	35.96	kPa	404.56	Calculated Property
Pvap	58.59	kPa	419.97	Calculated Property
Pvap	91.70	kPa	435.38	Calculated Property
Pvap	138.49	kPa	450.79	Calculated Property
Pvap	202.67	kPa	466.20	Calculated Property
Pvap	[1.59e-07; 2464.08]	kPa	[181.15; 616.00]	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			8.26165e+01
Coefficient B			-8.70435e+03
Coefficient C			-9.68492e+00
Coefficient D			4.03773e-06
Coefficient E			0.00000e+00
Temperature range, min.			181.15
Temperature range, max.			616.00
Pvap	1.59e-07	kPa	181.15	Calculated Property
Pvap	4.31e-04	kPa	229.47	Calculated Property
Pvap	0.05	kPa	277.78	Calculated Property
Pvap	1.36	kPa	326.10	Calculated Property
Pvap	12.78	kPa	374.42	Calculated Property
Pvap	65.71	kPa	422.73	Calculated Property
Pvap	226.67	kPa	471.05	Calculated Property
Pvap	595.90	kPa	519.37	Calculated Property
Pvap	1296.05	kPa	567.68	Calculated Property
Pvap	2464.08	kPa	616.00	Calculated Property

Similar Compounds

Find more compounds similar to Butanoic acid, butyl ester.

Mixtures

• Butanoic acid, butyl ester + Carbon dioxide
• Butanoic acid, butyl ester + Ethane, 1,2-dibromo-
• Butanoic acid, butyl ester + Propane, 1,3-dibromo-
• Butanoic acid, butyl ester + Butane, 1,4-dibromo-
• Butanoic acid, butyl ester + Pentane, 1,5-dibromo-
• Butanoic acid, butyl ester + 1,6-DIBROMOHEXANE
• Butanoic acid, butyl ester + Ethane, 1,2-dichloro-
• Butanoic acid, butyl ester + Propane, 1,3-dichloro-
• Butanoic acid, butyl ester + Butane, 1,4-dichloro-
• Butanoic acid, butyl ester + Pentane, 1,5-dichloro-
• Butanoic acid, butyl ester + Hexane, 1,6-dichloro-
• Butanoic acid, butyl ester + Acetic acid + Water
• Butanoic acid, butyl ester + Dodecane
• Butanoic acid, butyl ester + Dodecane + 1-Octanol
• Butanoic acid, butyl ester + Carbonic acid, dimethyl ester
• 2-Propanol, 2-methyl- + Butanoic acid, butyl ester

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Liquid-liquid equilibrium of water + acetic acid + butyl butyrate at 298 K and 1 atmosphere
• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides)III. HE m and V E m for 20 binary mixtures {xCu-1H2u-1CO2C4H9 + (1 - x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6
• Thermodynamic study of (alkyl esters + alpha,beta-alkyl dihalides) VI.H and V for 20 binary mixtures {xCu-1H2u-1CO2(CH2)3CH3 + (1 - x)alpha,omega-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, alpha = 1, and v = omega = 2 to 6
• Below the room temperature measurements of solubilities in ester absorbents for CO2 capture
• Measurement and Correlation of Vapor-Liquid Equilibrium for Binary Systems of Dimethyl Carbonate with Butyl Butyrate, o-Xylene, and Cyclohexanone at 101.3 kPa
• Excess molar volumes and enthalpies of mixing for the ternary system (butyl butyrate + 1-octanol + dodecane) at the temperature 308.15 K.
• Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
• Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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