Chemical Properties of Succinic anhydride (CAS 108-30-5)

InChI

InChI=1S/C4H4O3/c5-3-1-2-4(6)7-3/h1-2H2

InChI Key

RINCXYDBBGOEEQ-UHFFFAOYSA-N

Formula

C4H4O3

SMILES

O=C1CCC(=O)O1

Molecular Weight¹

100.07

CAS

108-30-5

Other Names

• 2,5(3H,4H)-Furandione
• 2,5-Diketotetrahydrofuran
• 2,5-Dioxotetrahydrofuran
• 2,5-Furandione, dihydro-
• Bernsteinsaure-anhydrid
• Butanedioic anhydride
• Dihydro-2,5-diketotetrahydrofuran
• Dihydro-2,5-furandione
• NCI-C55696
• NSC 8518
• Rikacid SA
• Succinic acid anhydride
• Succinyl anhydride
• Succinyl oxide
• Tetrahydro-2,5-dioxofuran
• Tetrahydro-2,5-furandione
• butanedioic acid, anhydride

• ω : Acentric Factor.
• Δ_cH°_solid : Standard solid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_solid : Solid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_subH° : Enthalpy of sublimation at standard conditions (kJ/mol).
• Δ_subH : Enthalpy of sublimation 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).
• I_np : Non-polar retention indices.
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.4413		Relay (1.0) Calculated Property
ΔcH°solid	[-1543.90; -1537.10]	kJ/mol
ΔcH°solid	-1537.10 ± 0.40	kJ/mol	NIST
ΔcH°solid	-1543.90 ± 0.63	kJ/mol	NIST
ΔfG°	-304.24	kJ/mol	Joback Calculated Property
ΔfH°gas	-527.90 ± 1.70	kJ/mol	NIST
ΔfH°solid	-608.60 ± 0.70	kJ/mol	NIST
ΔfusH°	5.98	kJ/mol	Joback Calculated Property
ΔsubH°	[80.70; 80.70]	kJ/mol
ΔsubH°	80.70 ± 1.60	kJ/mol	NIST
ΔsubH°	80.70 ± 1.60	kJ/mol	NIST
ΔsubH°	80.70	kJ/mol	NIST
ΔvapH°	48.57	kJ/mol	Relay (1.0) Calculated Property
IE	[10.80; 10.84]	eV
IE	10.84	eV	NIST
IE	10.84	eV	NIST
IE	10.84	eV	NIST
IE	10.80	eV	NIST
log10WS	-0.33		Relay (1.0) Calculated Property
logPoct/wat	-0.150		Crippen Calculated Property
McVol	65.370	ml/mol	McGowan Calculated Property
Pc	5670.27	kPa	Joback Calculated Property
Inp	1022.00		NIST
Tboil	534.20	K	NIST
Tc	708.14	K	Relay (1.0) Calculated Property
Tfus	[392.00; 393.17]	K
Tfus	393.17	K	Measurement and correlation of solubility of succinic anhydride in pure solvents and binary solvent mixtures
Tfus	392.60 ± 1.00	K	NIST
Tfus	393.15 ± 1.50	K	NIST
Tfus	392.00 ± 1.00	K	NIST
Vc	0.241	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[133.07; 184.46]	J/mol×K	[473.46; 717.29]
Cp,gas	133.07	J/mol×K	473.46	Joback Calculated Property
Cp,gas	142.43	J/mol×K	514.10	Joback Calculated Property
Cp,gas	151.55	J/mol×K	554.74	Joback Calculated Property
Cp,gas	160.37	J/mol×K	595.37	Joback Calculated Property
Cp,gas	168.82	J/mol×K	636.01	Joback Calculated Property
Cp,gas	176.87	J/mol×K	676.65	Joback Calculated Property
Cp,gas	184.46	J/mol×K	717.29	Joback Calculated Property
ΔsubH	[80.50; 82.20]	kJ/mol	[300.50; 309.00]
ΔsubH	82.20	kJ/mol	300.50	NIST
ΔsubH	80.50 ± 1.60	kJ/mol	309.00	NIST
ΔvapH	57.30	kJ/mol	467.50	NIST
Pvap	[20.00; 40.00]	kPa	[475.01; 499.14]
Pvap	20.00	kPa	475.01	Isobaric Vapor Liquid Equilibrium for Binary System of -Butyrolactone + Succinic Anhydride at 20.0, 30.0, and 40.0 kPa
Pvap	30.00	kPa	488.81	Isobaric Vapor Liquid Equilibrium for Binary System of -Butyrolactone + Succinic Anhydride at 20.0, 30.0, and 40.0 kPa
Pvap	40.00	kPa	499.14	Isobaric Vapor Liquid Equilibrium for Binary System of -Butyrolactone + Succinic Anhydride at 20.0, 30.0, and 40.0 kPa

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[0.87; 6722.70]	kPa	[393.00; 811.00]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.01282e+02
Coefficient B			-1.15330e+04
Coefficient C			-1.22030e+01
Coefficient D			5.30723e-06
Temperature range, min.			393.00
Temperature range, max.			811.00
Pvap	0.87	kPa	393.00	Calculated Property
Pvap	6.06	kPa	439.44	Calculated Property
Pvap	27.44	kPa	485.89	Calculated Property
Pvap	91.81	kPa	532.33	Calculated Property
Pvap	247.48	kPa	578.78	Calculated Property
Pvap	570.44	kPa	625.22	Calculated Property
Pvap	1172.85	kPa	671.67	Calculated Property
Pvap	2218.02	kPa	718.11	Calculated Property
Pvap	3946.85	kPa	764.56	Calculated Property
Pvap	6722.70	kPa	811.00	Calculated Property

Similar Compounds

Find more compounds similar to Succinic anhydride.

Mixtures

• Succinic anhydride + Tetrahydrofuran

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Measurement and correlation of solubility of succinic anhydride in pure solvents and binary solvent mixtures
• Isobaric Vapor Liquid Equilibrium for Binary System of -Butyrolactone + Succinic Anhydride at 20.0, 30.0, and 40.0 kPa
• Joback Method
• McGowan Method
• NIST Webbook

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