Conditions | Yield |
---|---|
With 5%-palladium/activated carbon; hydrogen In hexane; water at 100℃; under 20686.5 Torr; for 24h; Temperature; Pressure; Solvent; Reagent/catalyst; Sealed tube; | 99% |
Conditions | Yield |
---|---|
Photolysis; | |
With hydrogen; platinum | |
With Pt/γ-Al2O3; hydrogen at 160℃; Temperature; Gas phase; | |
With hydrogen at 100℃; under 750.075 Torr; for 3h; |
Conditions | Yield |
---|---|
With 0.3 wt. % palladium on alumina; hydrogen at 50℃; under 760.051 Torr; Fixed-bed flow reactor; | |
With hydrogen; calcium oxide at 130℃; under 760.051 Torr; Reagent/catalyst; Temperature; | |
With hydrogen In n-heptane at 17℃; under 7500.75 Torr; Autoclave; |
meso-erythritol
n-butane
Conditions | Yield |
---|---|
With tris(triphenylphosphine)ruthenium(II) chloride; hydrogen bromide; hydrogen; tetrabutyl phosphonium bromide In dodecane at 200℃; under 30003 Torr; for 4h; | 32% |
With hydrogen In water at 119.84℃; under 60006 Torr; for 144h; Autoclave; |
Conditions | Yield |
---|---|
With ruthenium (III) bromide; hydrogen bromide; hydrogen; tetra-n-butylphosphonium chloride In dodecane at 200℃; under 30003 Torr; for 4h; | A 51% B 8% |
1-butylene
carbon monoxide
A
methane
B
propane
C
Isobutane
D
n-butane
Conditions | Yield |
---|---|
With hydrogen; dodecacarbonyltetrairidium In various solvent(s) at 175℃; under 760 Torr; Further byproducts given; | A 0.5% B 16% C 59% D 11% |
propene
carbon monoxide
A
methane
B
propane
C
Isobutane
D
n-butane
Conditions | Yield |
---|---|
With hydrogen; dodecacarbonyltetrairidium In various solvent(s) at 175℃; under 760 Torr; Further byproducts given; | A 1% B 17% C 56% D 11% |
Conditions | Yield |
---|---|
With Pt/γ-Al2O3; hydrogen at 100℃; Temperature; Gas phase; | |
With hydrogen at 60℃; under 750.075 Torr; for 3h; | |
With platinum on silica gel; hydrogen at 400℃; under 760.051 Torr; | A 19 %Chromat. B 11 %Chromat. |
Conditions | Yield |
---|---|
With ethene; mercury In benzene-d6; water at -196 - 60℃; under 3040.2 Torr; Inert atmosphere; Glovebox; Sealed tube; Schlenk technique; | A 38% B 24% C 20% D 15% |
Conditions | Yield |
---|---|
With tertiary butyl chloride; tributylhexylphosphonium bromohexachloroaluminate at 95℃; under 8533.17 Torr; for 4.6h; Time; Autoclave; Inert atmosphere; | |
With tertiary butyl chloride; tributylhexylphosphonium bromohexachloroaluminate at 95℃; under 8533.17 Torr; for 4.6h; Time; Autoclave; Inert atmosphere; | |
With tertiary butyl chloride; tributylhexylphosphonium bromohexachloroaluminate at 95℃; under 8533.17 Torr; for 4.6h; Time; Autoclave; Inert atmosphere; |
buta-1,3-diene
A
1-butylene
B
(Z)-2-Butene
C
trans-2-Butene
D
n-butane
Conditions | Yield |
---|---|
With hydrogen; palladium In various solvent(s) at 40℃; under 3040 Torr; Kinetics; Product distribution; Further Variations:; Solvents; solvent-free; | A 72% B n/a C n/a D n/a |
With hydrogen; palladium dichloride In N,N-dimethyl-formamide under 18751.5 Torr; for 0.383333h; Product distribution; Ambient temperature; various time; | A 50% B 2.5% C 23% D 1% |
With hydrogen; LaPd3 at -38.1 - -0.1℃; Product distribution; Thermodynamic data; other catalyst; Ea; |
Conditions | Yield |
---|---|
With hydrogen; H-ZSM-5 (Si/Al 280) at 410℃; under 760.051 Torr; |
Conditions | Yield |
---|---|
With ruthenium (III) bromide; hydrogen bromide; hydrogen; tetrabutyl phosphonium bromide In dodecane at 200℃; under 30003 Torr; for 2h; Reagent/catalyst; | A 6% B 14% C 6% |
iso-butanol
n-butane
Conditions | Yield |
---|---|
With sulfuric acid; hydrogen In water at 99.84℃; under 60006 Torr; for 4h; | |
With hydrogen at 60 - 140℃; under 750.075 Torr; | |
Stage #1: iso-butanol Acidic conditions; Stage #2: With hydrogen at 60℃; under 750.075 Torr; |
Conditions | Yield |
---|---|
With isoprene In benzene-d6 at 60℃; Inert atmosphere; Glovebox; Sealed tube; | A 55% B 11% C 34% |
Conditions | Yield |
---|---|
With palladium on activated charcoal; hydrogen at 180℃; under 37503.8 Torr; for 2h; Temperature; Pressure; Autoclave; | 99% |
With pumice stone; nickel at 150 - 200℃; Hydrogenation; | |
With hydrogen; nickel at 180 - 200℃; | |
With C28H36Cl2Fe2O2P2; hydrogen In benzene-d6 at -195.16℃; under 3040.2 Torr; for 24h; Inert atmosphere; | |
With zeolite-acid |
Conditions | Yield |
---|---|
Pt/Al2O3 In water at 264.85℃; under 43128.4 Torr; | |
With hydrogenchloride; Pt/Al2O3 In water at 264.85℃; under 43128.4 Torr; pH=2; |
dichloromethane
ethylmagnesium chloride
A
propene
B
n-butane
C
pentane
Conditions | Yield |
---|---|
With C31H37ClN3NiO2(1-)*Li(1+) In tetrahydrofuran at 25℃; for 0.333333h; Inert atmosphere; Overall yield = 91 %; | A 14% B 20% C 57% |
Conditions | Yield |
---|---|
With ZnO-CeO2 mixed oxide at 399.84℃; under 760.051 Torr; for 1h; Temperature; Inert atmosphere; |
Conditions | Yield |
---|---|
With palladium on activated charcoal; hydrogen at 180℃; under 37503.8 Torr; for 2h; Temperature; Pressure; Autoclave; | 99% |
With pumice stone; nickel at 150 - 200℃; Hydrogenation; | |
With hydrogen; tetrahydrofuran; samarium at 20.9℃; under 135 Torr; |
Conditions | Yield |
---|---|
With helium; propene; hydrogen at 225℃; under 760.051 Torr; Catalytic behavior; Reagent/catalyst; Flow reactor; | 99.9% |
With hydrogen; aluminum oxide; sulfided Mo at 4℃; under 30 Torr; for 0.333333h; variation of reaction temperature; the reaction time was studied; | |
With hydrogen; Fe-Zr alloy Kinetics; |
thiophene
n-butane
Conditions | Yield |
---|---|
With hydrogen; aluminum oxide; cobalt; molybdenum at 400℃; Rate constant; gas phase; flow circulation apparatus; | |
With hydrogen; oceanic polymetallic nodules at 380 - 460℃; under 60004.8 - 82506.6 Torr; Kinetics; catalytic acivity, comparison with industrial catalysts; | |
With hydrogen; aluminum oxide; molybdenum at 420℃; under 760 Torr; for 24h; catalytic activities; different Mo contents and reaction times; effect of O2 or CO uptake to the rate of hydrogenolysis at 60 deg C or 0 deg C; |
Conditions | Yield |
---|---|
With hydrogenchloride; Pt/Al2O3 In water at 264.85℃; under 43128.4 Torr; pH=3; |
Conditions | Yield |
---|---|
With hydrogen; aluminum oxide; silica gel; palladium In water at 264.85℃; under 43653.5 Torr; pH=2; |
ethanol
A
diethyl ether
B
acetaldehyde
C
n-butane
D
butan-1-ol
Conditions | Yield |
---|---|
With hydrogen In water at 235℃; under 220.415 Torr; Reagent/catalyst; Guerbet Reaction; Flow reactor; |
Conditions | Yield |
---|---|
With aluminium oxide vanadium(V)-oxide catalyst at 380 - 400℃; under 29420.3 Torr; Hydrogenation; | |
With titanic acid at 430℃; | |
With hydrogen; vanadium(V) oxide; iron at 326.9℃; 1.5E5 Pa; Yield given; | |
With sulfuric acid; hydrogen In water at 99.84℃; under 60006 Torr; for 4h; |
Conditions | Yield |
---|---|
With sulfuric acid; hydrogen In water at 99.84℃; under 60006 Torr; for 4h; | |
With hydrogen In 1,4-dioxane at 139.84℃; under 60006 Torr; for 4h; Autoclave; |
carbon monoxide
A
ethane
B
propane
C
carbon dioxide
D
n-butane
Conditions | Yield |
---|---|
With hydrogen at 300℃; under 7500.75 Torr; for 10h; Reagent/catalyst; Temperature; |
Conditions | Yield |
---|---|
phosphotungstic acid; Al2O3-F; platinum at 310℃; Product distribution; Further Variations:; Catalysts; Temperatures; | A 0.6% B 62.1% C 0.6% |
With tertiary butyl chloride; C9H20N(1+)*Al2Cl7(1-) at 95℃; under 13446.2 Torr; for 4.4h; Time; Reagent/catalyst; Inert atmosphere; | A 30.79% B 21.33% C 8.72% |
aluminum tri-bromide; copper dichloride at 28℃; for 2h; Yield given; |
Conditions | Yield |
---|---|
With hydrogen; palladium/alumina In 1-methyl-pyrrolidin-2-one at 40℃; under 15001.5 Torr; Product distribution / selectivity; |
Conditions | Yield |
---|---|
With oxygen; vanadyl pyrophosphate at 420℃; | 100% |
With oxygen; vanadyl pyrophosphate at 420℃; Product distribution; other catalysts with different P/V atomic ratios and their catalityc activities investigated; | 100% |
With oxygen; vanadium-phosphorus oxidation catalyst at 396 - 491℃; Product distribution / selectivity; Gas phase; | 77% |
n-butane
2-nitrobutane
Conditions | Yield |
---|---|
With N-hydroxyphthalimide; air; Nitrogen dioxide In various solvent(s) at 100℃; under 1520.1 Torr; for 14h; | 65% |
With nitric acid at 420℃; 2-nitro-butane, inactive form; | |
With nitric acid at 205℃; | |
With nitric acid at 400 - 450℃; |
Conditions | Yield |
---|---|
With dipotassium peroxodisulfate; BF4(1-)*C24H51BCu3N3O16(1+)*2H2O; water In acetonitrile at 60℃; for 6h; Autoclave; | 26.7% |
With dipotassium peroxodisulfate; C26H38Cu3N4O16; water In acetonitrile at 60℃; for 6h; Reagent/catalyst; Autoclave; Green chemistry; | 25.4% |
With 2-pyrazylcarboxylic acid; dipotassium peroxodisulfate; ferrocene In water; acetonitrile at 60℃; under 7600.51 Torr; for 4h; Autoclave; | 19% |
methyl isoquinoline-3-carboxylate
n-butane
Conditions | Yield |
---|---|
With tris(2,2'-bipyridyl)ruthenium dichloride; 4,5,6,7-tetrafluoro-1-hydroxybenzo[d][1,2]iodaoxol-3(1H)-one In dichloromethane at 30℃; under 760.051 Torr; Minisci Aromatic Substitution; Inert atmosphere; Irradiation; chemoselective reaction; | 78% |
n-butane
A
butyraldehyde
B
butanone
C
iso-butanol
D
butyric acid
E
butan-1-ol
Conditions | Yield |
---|---|
With 2-pyrazylcarboxylic acid; ferrocene; dihydrogen peroxide; triphenylphosphine In acetonitrile at 50℃; for 4h; Autoclave; Overall yield = 58 %; | |
Stage #1: n-butane With 2-pyrazylcarboxylic acid; [{VO(EtO)(EtOH)}2(1κ2O,κN:2κ2O,κN-bis(2-hydroxybenzylidene)oxalohydrazonic acid)]·2H2O; dihydrogen peroxide In water; acetonitrile at 50℃; for 4h; Stage #2: With triphenylphosphine under 760.051 Torr; Autoclave; Overall yield = 45.3 %Chromat.; |
Conditions | Yield |
---|---|
With tetra-(n-butyl)ammonium iodide; sodium thiosulfate In water at 80℃; for 5h; Sealed tube; | 72% |
Conditions | Yield |
---|---|
magnesium-molybdenum | 98% |
With water; oxygen at 25 - 550℃; under 1800.18 - 11251.1 Torr; | 95% |
With water; hydrogen; oxygen at 25 - 555℃; under 1800.18 - 15001.5 Torr; Product distribution / selectivity; | 95% |
Conditions | Yield |
---|---|
With carbon dioxide at 540℃; Gas phase; Flow reactor; | 31% |
at 850℃; | |
at 800 - 850℃; | |
With gallium nitride at 450℃; under 0.00750075 Torr; |
Conditions | Yield |
---|---|
Stage #1: n-butane With oxygen at 403℃; under 2175.22 Torr; Stage #2: With hydrogen In Phthalic acid dibutyl ester Product distribution / selectivity; | 99.5% |
Conditions | Yield |
---|---|
With hydrogen at 380℃; under 2250.23 Torr; Temperature; | 62% |
With hydrogen; Pt-η-Al2O3-Cl at 200℃; under 15001.2 - 22501.8 Torr; Product distribution; test chlorinated catalysts for the isomerization of C4-C6 alkanes; also other alkanes (n-pentane, hexane fraction and their mixtures); | 53.83% |
With Ga(3+)-modified sulfated zirconia at 190℃; under 760.051 Torr; Reagent/catalyst; Flow reactor; | 30% |
Conditions | Yield |
---|---|
With oxygen; 12percentMo1Cs1Na0.04Pr0.01On/SiO2 at 475℃; under 760.051 Torr; |
Conditions | Yield |
---|---|
With C56H52ClFeN4O(1+) at 0℃; Kinetics; | 23% |
With hydrogen bromide; oxygen at 180℃; | |
With 2-pyrazylcarboxylic acid; dihydrogen peroxide; [n-Bu4N]VO3 In acetonitrile at 75℃; under 2280 Torr; for 2.5h; Product distribution; |
Butane (CAS NO.106-97-8) is reported in EPA TSCA Inventory.
OSHA PEL: TWA 800 ppm
ACGIH TLV: TWA 800 ppm
DFG MAK: 1000 ppm (2400 mg/m3)
DOT Classification: 2.1; Label: Flammable Gas
n-Butane, also known butane, is a highly flammable, colorless, easily liquefied gas with a faint petroleum-like odor. It is an alkane with four carbon atoms. Butane refers two structural isomers of n-butane and isobutane. It is insoluble in water, soluble in alcohol, ether, chloroform and other hydrocarbons. n-Butane is used primarily as gasoline blending components and less so as liquefied fuel and in the manufacture of chemicals.
Preparation: Oil field gas, wet natural gas and cracked gas all contain n-butane. So it can be obtained by separation.
1. Separation from oil field gas and wet natural gas: The propane and butane liquefied petroleum gas can be seperated by being pressurized and condensation. After distillation, butane is isolated.
2. Separation from cracked gas: The gas which is obtained from refinery by vacuum distillation at room temperature goes through the following reaction steps: reforming; catalytic cracking; coking; thermal cracking; hydrocracking. The obtained liquid gas can contain a large number of C4 fraction. Then, after reforming, hydrocracking and vacuum distillation, the C4 fraction is mainly butane (n-butane and isobutane). The by-product C4 fraction from ethylene unit also contains butane. After a series of treatment, n-butane (above 90%) can be obtained.
3. Use industrial cymogene (C4H10 80% ~ 90%) as raw material and molecular sieve as adsorbent for adsorption purification. The purity of 98% butane can be obtained. Use rectification to remove light components, the product purity can reach 99.99%.
Uses: n-Butane gas is sold bottled as a fuel for cooking and camping. When blended with propane as liquefied petroleum gas, it is largely used for heating homes, cooking and industrial heating. Pure butane gas is used in standard gas, calibration gas, aerosol spray regent, temperature and pressure gauges and ionizing particle counter. n-Butane is also used as fuel for cigarette lighters and portable stoves and as raw material for synthetic rubber and high octane liquid fluids. In addition, it is mainly used as raw material in organic synthesis. For example: after dehydrogenation, butylene and butadiene can be obtained; after isomerization iso-butane can be obtained; after catalytic oxidation, Maleic anhydride, acetic acid, acetaldehyde can be obtained; after halogenate, halogenated butane can be obtained; after nitration, nitrobutane can be obtained.
Safty: n-Butane is a kind of extremely flammable chemical. Therefore, you had better take the following instructions: Keep container in a well-ventilated place; Keep away from sources of ignition - No smoking. Inhalation of n-butane can cause asphyxia, euphoria, drowsiness, cardiac arrhythmia, narcosis, and frostbite, which can result in death from asphyxiation and ventricular fibrillation.
Structure Descriptors:
1. Smiles:C(CC)C
2. InChI:InChI=1/C4H10/c1-3-4-2/h3-4H2,1-2H3
Toxicity:
Organism | Test Type | Route | Reported Dose (Normalized Dose) | Effect | Source |
---|---|---|---|---|---|
mouse | LC50 | inhalation | 680gm/m3/2H (680000mg/m3) | Farmakologiya i Toksikologiya Vol. 30, Pg. 102, 1967. | |
rat | LC50 | inhalation | 658gm/m3/4H (658000mg/m3) | Farmakologiya i Toksikologiya Vol. 30, Pg. 102, 1967. |
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