- InChI
- InChI=1S/C5H8N4O12/c10-6(11)18-1-5(2-19-7(12)13,3-20-8(14)15)4-21-9(16)17/h1-4H2
- InChI Key
- TZRXHJWUDPFEEY-UHFFFAOYSA-N
- Formula
- C5H8N4O12
- SMILES
-
O=[N+]([O-])OCC(CO[N+](=O)[O-]
)(CO[N+](=O)[O-])CO[N+](=O)[O- ] - Molecular Weight1
- 316.14
- CAS
- 78-11-5
- Other Names
-
- 1,3-Propanediol, 2,2-bis((nitrooxy)methyl)-, 1,3-dinitrate
- 1,3-Propanediol, 2,2-bis[(nitrooxy)methyl]-, dinitrate
- 1,3-Propanediol, 2,2-bis[(nitrooxy)methyl]-, dinitrate (ester)
- 2,2-Bis[(nitrooxy)methyl]-1,3-propanediol dinitrate (ester)
- 2,2-bis(hydroxymethyl)-1,3-propanediol tetranitrate
- Angicap
- Angitet
- Antora
- Arcotrate
- Baritrate
- C 2
- C 2 (explosive)
- CHOT
- Cardiacap
- Deltrate-20
- Dilcoran-80
- Dipentrate
- Duotrate
- Erinit
- Extex
- Hasethrol
- Kaytrate
- Lentrat
- Lowetrate
- Martrate-45
- Metranil
- Mycardol
- Myotrate 10
- Neo-Corovas
- Neopentanetetrayl nitrate
- Niperyt
- Niperyth
- Nitrinal
- Nitrine
- Nitro-Riletten
- Nitrolong
- Nitropent
- Nitropenta
- Nitropenta 7W
- Nitropentaerythrite
- Nitropentaerythritol
- Nitropenton
- Nitrotalans
- P.E.T.N.
- PETN
- PETN (pentaerythritol tetranitrate)
- Pen-Tetra
- Pencard
- Pentaerithrityl Tetranitrate
- Pentaerythrityl tetranitrate
- Pentafilin
- Pentafin
- Pentanitrine
- Pentanitrol
- Pentestan-80
- Pentetrate Unicelles
- Penthrit
- Penthrite
- Pentitrate
- Pentral 80
- Pentrate
- Pentrinat
- Pentrite
- Pentritol
- Pentritol tempules
- Pentryate
- Pergitral
- Peridex
- Peridex-LA
- Peritrate
- Perityl
- Prevangor
- Quintrate
- Rythritol
- Subicard
- TEN
- Tanipent
- Tena
- Tentrate-20
- Terpate
- Tetranitropentaerythrite
- Tetranitropentaerythritol
- Tetrasule
- Tranite D-Lay
- Vaso-80 Unicelles
- Vasodiatol
- Vasolat
- XTX 8003
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°solid : Solid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔsubH° : Enthalpy of sublimation at standard conditions (kJ/mol).
- ΔsubH : Enthalpy of sublimation at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Psub : Sublimation pressure (kPa).
- Inp : Non-polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°solid | [-2572.40; -2569.80] | kJ/mol |
|
| ΔcH°solid | -2572.40 ± 0.80 | kJ/mol | NIST |
| ΔcH°solid | -2569.80 ± 2.50 | kJ/mol | NIST |
| ΔfG° | -283.74 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -727.20 | kJ/mol | Joback Calculated Property |
| ΔfH°solid | -538.50 ± 0.80 | kJ/mol | NIST |
| ΔfusH° | 51.49 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [150.40; 152.00] | kJ/mol |
|
| ΔsubH° | 150.40 ± 1.30 | kJ/mol | NIST |
| ΔsubH° | 152.00 ± 2.00 | kJ/mol | NIST |
| ΔvapH° | 101.43 | kJ/mol | Joback Calculated Property |
| log10WS | -2.32 | Crippen Calculated Property | |
| logPoct/wat | -1.194 | Crippen Calculated Property | |
| McVol | 174.470 | ml/mol | McGowan Calculated Property |
| Pc | 3464.28 | kPa | Joback Calculated Property |
| Inp | [1785.00; 1813.94] |
|
|
| Inp | 1805.54 | NIST | |
| Inp | 1813.94 | NIST | |
| Inp | 1791.00 | NIST | |
| Inp | 1785.00 | NIST | |
| Inp | 1791.00 | NIST | |
| Inp | 1791.00 | NIST | |
| Inp | 1805.54 | NIST | |
| Inp | 1785.00 | NIST | |
| Tboil | 1007.61 | K | Joback Calculated Property |
| Tc | 1272.59 | K | Joback Calculated Property |
| Tfus | 414.10 | K | Melting... |
| Vc | 0.705 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [538.50; 546.27] | J/mol×K | [1007.61; 1272.59] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 538 540 542 544 546 1100 1200 | ||||
| Cp,gas | 538.50 | J/mol×K | 1007.61 | Joback Calculated Property |
| Cp,gas | 542.46 | J/mol×K | 1051.77 | Joback Calculated Property |
| Cp,gas | 545.06 | J/mol×K | 1095.94 | Joback Calculated Property |
| Cp,gas | 546.27 | J/mol×K | 1140.10 | Joback Calculated Property |
| Cp,gas | 546.09 | J/mol×K | 1184.26 | Joback Calculated Property |
| Cp,gas | 544.50 | J/mol×K | 1228.43 | Joback Calculated Property |
| Cp,gas | 541.50 | J/mol×K | 1272.59 | Joback Calculated Property |
| ΔsubH | [151.90; 156.90] | kJ/mol | [369.00; 390.50] |
|
| ΔsubH | 156.90 ± 0.80 | kJ/mol | 369.00 | NIST |
| ΔsubH | 151.90 ± 2.10 | kJ/mol | 390.50 | NIST |
| Psub | [2.31e-09; 1.15e-03] | kPa | [302.20; 382.00] |
|
|
T(K) Sublimation pressure (kPa) 0 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 320 340 360 380 | ||||
| Psub | 2.31e-09 | kPa | 302.20 | Sublima... |
| Psub | 9.50e-09 | kPa | 310.00 | Sublima... |
| Psub | 3.02e-08 | kPa | 315.00 | Sublima... |
| Psub | 1.64e-07 | kPa | 325.40 | Sublima... |
| Psub | 3.59e-07 | kPa | 329.00 | Sublima... |
| Psub | 7.31e-07 | kPa | 333.00 | Sublima... |
| Psub | 4.08e-06 | kPa | 343.30 | Sublima... |
| Psub | 5.41e-06 | kPa | 344.80 | Sublima... |
| Psub | 1.28e-05 | kPa | 350.10 | Sublima... |
| Psub | 2.17e-05 | kPa | 353.30 | Sublima... |
| Psub | 3.01e-05 | kPa | 356.10 | Sublima... |
| Psub | 3.53e-05 | kPa | 356.90 | Sublima... |
| Psub | 6.42e-05 | kPa | 361.10 | Sublima... |
| Psub | 7.50e-05 | kPa | 361.90 | Sublima... |
| Psub | 8.52e-05 | kPa | 363.20 | Sublima... |
| Psub | 1.77e-04 | kPa | 368.10 | Sublima... |
| Psub | 2.04e-04 | kPa | 368.90 | Sublima... |
| Psub | 2.08e-04 | kPa | 369.20 | Sublima... |
| Psub | 2.30e-04 | kPa | 370.00 | Sublima... |
| Psub | 3.42e-04 | kPa | 373.00 | Sublima... |
| Psub | 4.46e-04 | kPa | 374.90 | Sublima... |
| Psub | 4.86e-04 | kPa | 376.20 | Sublima... |
| Psub | 5.76e-04 | kPa | 376.60 | Sublima... |
| Psub | 7.62e-04 | kPa | 379.00 | Sublima... |
| Psub | 9.44e-04 | kPa | 380.50 | Sublima... |
| Psub | 9.58e-04 | kPa | 380.80 | Sublima... |
| Psub | 1.15e-03 | kPa | 382.00 | Sublima... |
Similar Compounds
![1,3-Propanediol, 2-methyl-2-[(nitrooxy)methyl]-, dinitrate (ester).](data:image/png;base64,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)
Find more compounds similar to Pentaerythritol Tetranitrate.
Sources
- Crippen Method
- Crippen Method
- Melting Behavior and Heat of Fusion of Compounds that Undergo Simultaneous Melting and Decomposition: An investigation with HMX
- Sublimation Pressure and Vapor Molecular Weight of Pentaerythritol Tetranitrate
- Joback Method
- McGowan Method
- NIST Webbook
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