Heptane
Structural formula | ||||||||||||||||
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General | ||||||||||||||||
Surname | Heptane | |||||||||||||||
other names |
n -heptane |
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Molecular formula | C 7 H 16 | |||||||||||||||
Brief description |
colorless liquid with a faint gasoline odor |
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External identifiers / databases | ||||||||||||||||
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properties | ||||||||||||||||
Molar mass | 100.21 g mol −1 | |||||||||||||||
Physical state |
liquid |
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density |
0.68 g cm −3 |
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Melting point |
−91 ° C |
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boiling point |
98 ° C |
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Vapor pressure |
47.4 h Pa (20 ° C) |
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solubility |
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Refractive index |
1.3878 |
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safety instructions | ||||||||||||||||
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MAK |
500 ml m −3 , 2100 mg m −3 |
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As far as possible and customary, SI units are used. Unless otherwise noted, the data given apply to standard conditions . Refractive index: Na-D line , 20 ° C |
Heptane | |
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Brief description | Reference fuel (RON = 0 by definition) |
properties | |
Physical state | liquid |
calorific value |
8.5 kWh / L = 12.5 kWh / kg |
Octane number |
0 RON (by definition) |
Flash point |
−7 ° C |
Ignition temperature | 220 ° C |
Explosive limit | 0.84-6.7% by volume |
Temperature class | T3 |
Explosion class | IIA |
safety instructions | |
UN number | 1206 |
Hazard number | 33 |
As far as possible and customary, SI units are used. Unless otherwise noted, the data given apply to standard conditions . |
Heptane is a chain-like hydrocarbon from the substance group of alkanes having the empirical formula C 7 H 16 . He is the unbranched representatives of nine heptane - isomers . Heptane is flammable and hazardous to water ( WGK 2).
Occurrence and extraction
Heptane occurs naturally in crude oil from which it is obtained by distillation . It is also found in the essential oils of some pines and in the fruits of Pittosporum resiniferum (so-called petroleum nuts ) that are common in the Philippines .
properties
Physical Properties
Heptane is a clear, low-viscosity liquid that boils at 98 ° C at normal pressure. The vapor pressure function results according to Antoine according to log 10 (P) = A− (B / (T + C)) (P in bar, T in K) with A = 4.81803, B = 1635.409 and C = −27.338 in the temperature range from 185.3 to 295.6 K and with A = 4.02832, B = 1268.636 and C = −56.199 in the temperature range from 299.1 to 372.4 K. The temperature dependence of the enthalpy of vaporization can be determined according to the equation Δ V H 0 = Aexp (−βT r ) (1 − T r ) β (Δ V H 0 in kJ / mol, T r = (T / T c ) reduced temperature) with A = 53.66 kJ / mol, Describe β = 0.2831 and T c = 540.2 K in the temperature range between 298 K and 363 K. With 2.2 mg · l −1 at 25 ° C , heptane is only very slightly soluble in water. The calorific value is 44.7 MJ / kg.
Heptane vapor pressure function
Temperature dependence of the heat of vaporization of heptane
The compound forms azeotropically boiling mixtures with a number of other solvents . The azeotropic compositions and boiling points can be found in the following table. No azeotropes are formed with cyclohexane , hexane , toluene , ethylbenzene , xylene , cyclohexanol, and carbon disulfide .
Azeotropes with various solvents | ||||||
solvent | water | Methanol | Ethanol | 1-propanol | 2-propanol | |
Content of heptane | in% | 87 | 59 | 51 | 64 | 50 |
boiling point | in ° C | 79 | 49 | 71 | 88 | 76 |
solvent | Ethylene glycol methyl ether | Ethylene glycol ethyl ether | acetone | Methyl ethyl ketone | Methyl isobutyl ketone | |
Content of heptane | in% | 77 | 86 | 10 | 30th | 87 |
boiling point | in ° C | 92 | 97 | 56 | 77 | 98 |
solvent | 1-butanol | i -butanol | 2-butanol | Ethanediol | Acetonitrile | |
Content of heptane | in% | 82 | 73 | 62 | 97 | 54 |
boiling point | in ° C | 94 | 91 | 89 | 98 | 69 |
solvent | Dioxane | Methyl acetate | Ethyl acetate | Isopropyl acetate | DMF | |
Content of heptane | in% | 56 | 3 | 6th | 33 | 95 |
boiling point | in ° C | 92 | 57 | 77 | 88 | 97 |
Safety-related parameters
Heptane forms highly flammable vapor-air mixtures. The compound has a flash point of −7 ° C. The explosion range is between 0.84% by volume (35 g / m³) as the lower explosion limit (LEL) and 6.7% by volume (280 g / m³) as the upper explosion limit (UEL). A correlation of the explosion limits with the vapor pressure function results in a lower explosion point of −8 ° C and an upper explosion point of 27 ° C. The maximum explosion pressure is 9.4 bar. The limit gap width was determined to be 0.91 mm. This results in an assignment to explosion group IIA. With a minimum ignition energy of 0.24 mJ, vapor-air mixtures are extremely ignitable. The ignition temperature is 220 ° C. The substance therefore falls into temperature class T3. The electrical conductivity is very low at 7.0 · 10 −14 S · m −1 .
According to the dangerous goods regulations , heptane is assigned to class 3 (flammable liquids) with packing group II (medium hazard) and UN number 1206 (label: 3).
use
Heptane is used as a non-polar solvent in organic synthesis. Since the compound is very easy on knocking, it is used with the octane number "RON = 0" as one of the two comparison fuels in addition to the knock- proof isooctane ("RON = 100") for determining the octane number .
n-Heptane is the main component of some start-up sprays .
1-Bromoheptane can be obtained by brominating n-heptane .
Individual evidence
- ↑ a b c d e f g h i j k l m n o p q r s entry on heptane in the GESTIS substance database of the IFA , accessed on July 26, 2019(JavaScript required) .
- ↑ a b entry on heptane. In: Römpp Online . Georg Thieme Verlag, accessed on December 28, 2014.
- ^ CRC Handbook of Chemistry and Physics , 57. Edition, CRC Press, Boca Raton, Florida, 1976, Section C, Physical Constants of Organic Compounds , pp. C-328.
- ↑ Entry on Heptane in the Classification and Labeling Inventory of the European Chemicals Agency (ECHA), accessed on February 1, 2016. Manufacturers or distributors can expand the harmonized classification and labeling .
- ↑ a b c d e f g h E. Brandes, W. Möller: Safety-related parameters - Volume 1: Flammable liquids and gases , Wirtschaftsverlag NW - Verlag für neue Wissenschaft GmbH, Bremerhaven 2003.
- ↑ K. Griesbaum, A. Behr, D. Biedenkapp, H.-W. Voges, D. Garbe, C. Paetz, G. Collin, D. Mayer, H. Höke: Hydrocarbons in Ullmann's Encyclopedia of Industrial Chemistry, 2012 Wiley-VCH Verlag GmbH & Co, Weinheim, doi : 10.1002 / 14356007.a13_227 .
- ↑ Carruth, GF; Kobayashi, R .: Vapor Pressure of Normal Paraffins Ethane Through n -Decane from Their Triple Points to About 10 Mm Hg in J. Chem. Eng. Data 18 (1973) 115-126, doi: 10.1021 / je60057a009 .
- ↑ Williamham, CB; Taylor, WJ; Pignocco, JM; Rossini, FD: Vapor Pressures and Boiling Points of Some Paraffin, Alkylcyclopentane, Alkylcyclohexane, and Alkylbenzene Hydrocarbons in J. Res. Natl. Bur. Stand. (US) 35 (1945) 219-244.
- ↑ Majer, V .; Svoboda, V .: Enthalpies of Vaporization of Organic Compounds: A Critical Review and Data Compilation , Blackwell Scientific Publications, Oxford, 1985, 300.
- ↑ a b I.M. Smallwood: Handbook of organic solvent properties , Arnold London 1996, ISBN 0-340-64578-4 , pp. 12-13.
- ↑ Technical rule for operational safety - TRBS 2153, BG RCI leaflet T033 Avoidance of ignition hazards due to electrostatic charges , as of April 2009, Jedermann-Verlag Heidelberg.
- ^ H. Altenburg, I. Bang, K. Bartelt, Fr. Baum, C. Brahm, W. Cramer, K. Dieterich, R. Ditmar, M. Dohrn, H. Einbeck, H. Euler, ES Faust, C. Funk, O. v. Fürth, O. Gerngroß: Biochemisches Handlexikon 1st volume, 1st half carbon, hydrocarbons, alcohols of the aliphatic series, phenols . Springer-Verlag, 2013, ISBN 978-3-642-90817-0 , pp. 101 ( limited preview in Google Book search).