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Isobutane, also known as methylpropane, is a chemical compound with the molecular formula C4H10. It is a hydrocarbon and an isomer of butane. This colorless, odorless gas at room temperature has a variety of applications across different industries due to its unique properties.

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  • 75-28-5 Structure
  • Basic information

    1. Product Name: Isobutane
    2. Synonyms: 1,1-Dimethylethane;A 31 (hydrocarbon);Isobutane;Purifrigor Iso 2;Purifrigor Iso 2.5;Purifrigor Iso 3;Purifrigor Iso 3.5;R 600a;Trimethylmethane;iso-Butane;
    3. CAS NO:75-28-5
    4. Molecular Formula: C4H10
    5. Molecular Weight: 58.14
    6. EINECS: 200-857-2
    7. Product Categories: N/A
    8. Mol File: 75-28-5.mol
    9. Article Data: 447
  • Chemical Properties

    1. Melting Point: N/A
    2. Boiling Point: −12 °C(lit.)
    3. Flash Point: -83 °C
    4. Appearance: a kind of air with no odour and no color
    5. Density: 0.612 g/cm3
    6. Refractive Index: N/A
    7. Storage Temp.: N/A
    8. Solubility: N/A
    9. CAS DataBase Reference: Isobutane(CAS DataBase Reference)
    10. NIST Chemistry Reference: Isobutane(75-28-5)
    11. EPA Substance Registry System: Isobutane(75-28-5)
  • Safety Data

    1. Hazard Codes: N/A
    2. Statements: N/A
    3. Safety Statements: N/A
    4. WGK Germany:
    5. RTECS:
    6. HazardClass: N/A
    7. PackingGroup: N/A
    8. Hazardous Substances Data: 75-28-5(Hazardous Substances Data)

75-28-5 Usage

Uses

Used in Aerosol Propellants:
Isobutane is used as a propellant in aerosol cans and foam products, providing a means to dispense substances in a controlled manner. Its effectiveness in this application is due to its ability to create pressure within the container, allowing for the even distribution of the product.
Used in Refrigeration Systems:
Isobutane is utilized in refrigeration systems as a coolant, taking advantage of its high heat of vaporization. This property enables it to absorb and release heat efficiently, making it an effective component in maintaining low temperatures in various cooling applications.
Used in Chemical Industry:
Isobutane is used as a raw material in the production of various chemicals, such as isobutene, which is an important intermediate in the synthesis of rubber and plastics. Its versatility as a feedstock in the chemical industry is due to its reactivity and the ease with which it can be converted into other useful compounds.
Used in Fuel Industry:
Isobutane is used as a component in gasoline, contributing to its energy content and performance. Its presence in fuel mixtures can improve the combustion process, leading to more efficient and cleaner burning.
Used in Medical Industry:
Isobutane is used as a refrigerant in certain medical applications, such as cryotherapy, where its ability to absorb heat rapidly is beneficial for cooling tissues during surgical procedures or for treating certain skin conditions. Its properties make it a valuable asset in these specialized applications.

Check Digit Verification of cas no

The CAS Registry Mumber 75-28-5 includes 5 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 2 digits, 7 and 5 respectively; the second part has 2 digits, 2 and 8 respectively.
Calculate Digit Verification of CAS Registry Number 75-28:
(4*7)+(3*5)+(2*2)+(1*8)=55
55 % 10 = 5
So 75-28-5 is a valid CAS Registry Number.
InChI:InChI=1/C4H10/c1-4(2)3/h4H,1-3H3

75-28-5 Well-known Company Product Price

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  • Detail
  • Aldrich

  • (539821)  2-Methylpropane  99.995%

  • 75-28-5

  • 539821-170G

  • 5,713.11CNY

  • Detail

75-28-5SDS

SAFETY DATA SHEETS

According to Globally Harmonized System of Classification and Labelling of Chemicals (GHS) - Sixth revised edition

Version: 1.0

Creation Date: Aug 16, 2017

Revision Date: Aug 16, 2017

1.Identification

1.1 GHS Product identifier

Product name isobutane

1.2 Other means of identification

Product number -
Other names Propane, 2-methyl-

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only. Food additives
Uses advised against no data available

1.4 Supplier's details

1.5 Emergency phone number

Emergency phone number -
Service hours Monday to Friday, 9am-5pm (Standard time zone: UTC/GMT +8 hours).

More Details:75-28-5 SDS

75-28-5Synthetic route

tripotassiumdecaisobutylpentaaluminum

tripotassiumdecaisobutylpentaaluminum

deuterium cation

deuterium cation

A

Isobutane
75-28-5

Isobutane

B

potassium ion

potassium ion

C

deuterium
16873-17-9

deuterium

D

Al(OH)2(1+)

Al(OH)2(1+)

Conditions
ConditionsYield
With water In water byproducts: H2, HD; acid hydrolysis with 20% DCl (84%); quantities of the products determined;A n/a
B 100%
C n/a
D n/a
tripotassiumdecaisobutylpentaaluminum

tripotassiumdecaisobutylpentaaluminum

hydrogen cation

hydrogen cation

A

Isobutane
75-28-5

Isobutane

B

potassium ion

potassium ion

C

hydrogen
1333-74-0

hydrogen

D

Al(OH)2(1+)

Al(OH)2(1+)

Conditions
ConditionsYield
With water In water acid hydrolysis with 20% HCl; quantities of the products determined;A n/a
B 100%
C n/a
D n/a
tert-butyl alcohol
75-65-0

tert-butyl alcohol

A

Isobutane
75-28-5

Isobutane

B

triptane
464-06-2

triptane

Conditions
ConditionsYield
With triisopropylborane; trifluorormethanesulfonic acid In 1,1,2-Trichloro-1,2,2-trifluoroethane 1.) -30 deg C, 30 min 2.) room temp., 6 h;A 99.9%
B 0.1%
pivaloyl chloride
3282-30-2

pivaloyl chloride

Isobutane
75-28-5

Isobutane

Conditions
ConditionsYield
With tris-(trimethylsilyl)silane; 2,2'-azobis(isobutyronitrile) In toluene at 80℃; for 0.5h;98%
triethyl borane
97-94-9

triethyl borane

tert-butyl alcohol
75-65-0

tert-butyl alcohol

A

Isobutane
75-28-5

Isobutane

B

2,2-Dimethylbutane
75-83-2

2,2-Dimethylbutane

Conditions
ConditionsYield
With trifluorormethanesulfonic acid In 1,1,2-Trichloro-1,2,2-trifluoroethane 1.) -30 deg C 2.) room temp.;A 92.5%
B 7.5%
vanadocene

vanadocene

t-butyl bromide
507-19-7

t-butyl bromide

A

vanadocene monobromide

vanadocene monobromide

B

Isobutane
75-28-5

Isobutane

C

hydrogen
1333-74-0

hydrogen

D

isobutene
115-11-7

isobutene

Conditions
ConditionsYield
In hexane room temp.; further products:t-butylcyclopentadiene, tetramethylbutane, 2-methyl-4,4-dimethyl-1-pentene; GCL;A 92%
B n/a
C n/a
D n/a

A

Isobutane
75-28-5

Isobutane

B

n-butane
106-97-8

n-butane

Conditions
ConditionsYield
With aluminium trichloride; polyethoxysilane (silicone GKZh-94) In nitromethane Product distribution;A 6%
B 91%
2,2-dimethylpropane
463-82-1

2,2-dimethylpropane

A

methane
34557-54-5

methane

B

ethane
74-84-0

ethane

C

propane
74-98-6

propane

D

Isobutane
75-28-5

Isobutane

E

methylbutane
78-78-4

methylbutane

Conditions
ConditionsYield
With hydrogen; platinum at 243℃; Product distribution; further reaction temperatures, catalysts;A 2.7%
B 1.5%
C 1.5%
D 6.7%
E 87.8%
at 304℃; Product distribution; also from n-butane, other products,other temperatures, other catalysts;A 7%
B 1.7%
C 2.4%
D 15.6%
E 73.3%
With hydrogen; NaY-500; palladium at 216℃; Product distribution; Kinetics; Thermodynamic data; other catalysts, other temperatures; activation energies;
With hydrogen In neat (no solvent) at 275℃; under 1225.5 Torr; Reagent/catalyst; Inert atmosphere;
tetraisobutyl stannane
3531-43-9

tetraisobutyl stannane

A

propane
74-98-6

propane

B

Isobutane
75-28-5

Isobutane

C

isobutene
115-11-7

isobutene

D

n-butane
106-97-8

n-butane

Conditions
ConditionsYield
With hydrogen byproducts: C5 hydrocarbons, paraffin; 20 h, 300-310°C, 100 atm;A 1.6%
B 85.7%
C 2.5%
D 3.1%
With H2 byproducts: C5 hydrocarbons, paraffin; 20 h, 300-310°C, 100 atm;A 1.6%
B 85.7%
C 2.5%
D 3.1%
{bis(triphenylphosphine)nitrogen}{HW(CO)5}
78709-76-9

{bis(triphenylphosphine)nitrogen}{HW(CO)5}

t-butyl bromide
507-19-7

t-butyl bromide

A

bromopentacarbonyl tungstate(0)(1-)
15131-04-1

bromopentacarbonyl tungstate(0)(1-)

B

Isobutane
75-28-5

Isobutane

Conditions
ConditionsYield
In tetrahydrofuran Kinetics; 26.0°C, 20-fold excess of alkyl halide; second-order rate const. is given; anal. of the reaction mixt. by gas chromy.;A n/a
B 81%
bis(η3-2-methylallyl)nickel

bis(η3-2-methylallyl)nickel

Isobutane
75-28-5

Isobutane

Conditions
ConditionsYield
With hydrogen79.5%
With H279.5%
With hydrogen79.5%
butan-1-ol
71-36-3

butan-1-ol

A

Isobutane
75-28-5

Isobutane

B

n-butane
106-97-8

n-butane

Conditions
ConditionsYield
With aluminium trichloride; polyethoxysilane (silicone GKZh-94) In nitromethane Product distribution;A 4%
B 78%
2,4,6-tri-t-butylphenyl-fluoro-(ethylamino)borane
152240-85-2

2,4,6-tri-t-butylphenyl-fluoro-(ethylamino)borane

A

2,4,6-tri-t-butylphenyl-(ethylimino)borane
152240-88-5

2,4,6-tri-t-butylphenyl-(ethylimino)borane

B

Isobutane
75-28-5

Isobutane

Conditions
ConditionsYield
With tert.-butyl lithium In hexane byproducts: LiF; dropping a soln. of t-butyl lithium in n-hexane to a soln. of 2,4,6-tri-t-butylphenyl-fluoro-(ethylamino)borane in n-hexane under N2 at -50°C and allowing to stand overnight; removal of the solvent under reduced pressure and subliming the iminoborane from the residue in an oil pump vacuum, elem. anal.;A 78%
B n/a
adamantylamino-2,4,6-tri-t-butylphenyl fluoroborane
152240-83-0

adamantylamino-2,4,6-tri-t-butylphenyl fluoroborane

A

(adamantylimino)-2,4,6-tri-t-butylphenyl-borane
152240-90-9

(adamantylimino)-2,4,6-tri-t-butylphenyl-borane

B

Isobutane
75-28-5

Isobutane

Conditions
ConditionsYield
With tert.-butyl lithium In hexane byproducts: LiF; dropping a soln. of t-butyl lithium in n-hexane to a soln. of adamantylamino-2,4,6-tri-t-butylphenyl-fluoroborane in n-hexane under N2 at -50°C, allowing to stand overnight and refluxing for 12 h; removal of the solvent under reduced pressure and subliming the iminoborane from the residue in an oil pump vacuum, elem. anal.;A 73%
B n/a
diethyl(2,2'-bipyridyl)nickel(II)
15218-76-5

diethyl(2,2'-bipyridyl)nickel(II)

tertiary butyl chloride
507-20-0

tertiary butyl chloride

A

dichloro(2,2'-bipyridine)nickel(II)
22775-90-2

dichloro(2,2'-bipyridine)nickel(II)

B

ethane
74-84-0

ethane

C

Isobutane
75-28-5

Isobutane

D

isobutene
115-11-7

isobutene

E

n-butane
106-97-8

n-butane

Conditions
ConditionsYield
In neat (no solvent) t-BuCl added by trap-to-trap distn. to NiEt2(bpy), stirred at room temp. for 3 d; evapd. in vac.; GLC anal.;A 70%
B 2%
C 4%
D 50%
E 64%
methylbutane
78-78-4

methylbutane

A

propane
74-98-6

propane

B

Isobutane
75-28-5

Isobutane

Conditions
ConditionsYield
With aluminum oxide; silica gel; boron trichloride at 59.85℃; Product distribution;A 1.8%
B 68.8%
2-Methylpentane
107-83-5

2-Methylpentane

A

2-Methylhexane
591-76-4

2-Methylhexane

B

methane
34557-54-5

methane

C

ethane
74-84-0

ethane

D

propane
74-98-6

propane

E

Isobutane
75-28-5

Isobutane

F

methylbutane
78-78-4

methylbutane

Conditions
ConditionsYield
With hydrogen; tungsten film at 223.9℃; Product distribution; various temperature;A 0.2%
B n/a
C n/a
D 1.5%
E 1.4%
F 65.8%
(η5-pentamethylcyclopentadienyl)2(zirconium)(H)(iosbutyl)2
67108-86-5

(η5-pentamethylcyclopentadienyl)2(zirconium)(H)(iosbutyl)2

A

Cp'2Zr(H)Ph
112532-20-4

Cp'2Zr(H)Ph

B

Isobutane
75-28-5

Isobutane

Conditions
ConditionsYield
With benzene In benzene Irradiation (UV/VIS); (C5Me5)2Zr(H)CH2CH(CH3) in benzene is degassed and photolyzed with a blacklight for 10 days (vac.).; Evapn., addn. of petroleum ether at -78°C, stirring for several hours, cold filtn. of yellow solid, washing (cold petroleum ether), recrystn. (-78°C, petroleum ether), elem. anal.;A 65.6%
B n/a
2-methyl-propan-1-ol
78-83-1

2-methyl-propan-1-ol

A

Isobutane
75-28-5

Isobutane

B

n-butane
106-97-8

n-butane

Conditions
ConditionsYield
With aluminium trichloride; polyethoxysilane (silicone GKZh-94) In nitromethane Product distribution;A 64%
B 26%
pentane
109-66-0

pentane

A

Isobutane
75-28-5

Isobutane

B

methylbutane
78-78-4

methylbutane

Conditions
ConditionsYield
With aluminum oxide; silica gel; boron trichloride at 59.85℃; Product distribution; Further Variations:; Reagents;A 8%
B 64%
Sulfate; tin(IV) oxide at 249.9℃; Product distribution; pulse reactor; catalyst activity studied, prep. of catalyst varied;A 7.5%
B 3%
aluminum oxide; boron trifluoride at 19.9℃; under 201.02 Torr; Rate constant; different catalytic systems, different BF3-pressure;
pentane
109-66-0

pentane

A

Isobutane
75-28-5

Isobutane

B

methylbutane
78-78-4

methylbutane

C

n-butane
106-97-8

n-butane

Conditions
ConditionsYield
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;
n-butane
106-97-8

n-butane

Isobutane
75-28-5

Isobutane

Conditions
ConditionsYield
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%
chloroform
67-66-3

chloroform

butyl magnesium bromide
693-04-9

butyl magnesium bromide

A

2,4-dimethylpentane
108-08-7

2,4-dimethylpentane

B

Isobutane
75-28-5

Isobutane

Conditions
ConditionsYield
With C31H37ClN3NiO2(1-)*Li(1+) In tetrahydrofuran at 25℃; for 0.333333h; Inert atmosphere; Overall yield = 96.3 %;A 62%
B 34.3%
propane
74-98-6

propane

A

ethane
74-84-0

ethane

B

Isobutane
75-28-5

Isobutane

C

n-butane
106-97-8

n-butane

D

pentane
109-66-0

pentane

Conditions
ConditionsYield
silica/alumina-supp. -O-W[(C-tBu)(-CH2-tBu)2] at 150℃; under 600 Torr; for 120h; Product distribution; Further Variations:; Catalysts;A 61.7%
B 3.4%
C 25.7%
D 5.5%
tert-butylaluminum sesquibromide

tert-butylaluminum sesquibromide

Isobutane
75-28-5

Isobutane

Conditions
ConditionsYield
With water61%
Rh(PPh3)2(μ-N,O-2-pyridone-[Al(iBu)2(NO3)])(CO)

Rh(PPh3)2(μ-N,O-2-pyridone-[Al(iBu)2(NO3)])(CO)

Isobutane
75-28-5

Isobutane

Conditions
ConditionsYield
With hydrogen In benzene-d6 at 24.84℃; under 760.051 Torr; Kinetics; Mechanism; Pressure;60%
1-butylene
106-98-9

1-butylene

carbon monoxide
201230-82-2

carbon monoxide

A

methane
34557-54-5

methane

B

propane
74-98-6

propane

C

Isobutane
75-28-5

Isobutane

D

n-butane
106-97-8

n-butane

Conditions
ConditionsYield
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
187737-37-7

propene

carbon monoxide
201230-82-2

carbon monoxide

A

methane
34557-54-5

methane

B

propane
74-98-6

propane

C

Isobutane
75-28-5

Isobutane

D

n-butane
106-97-8

n-butane

Conditions
ConditionsYield
With hydrogen; dodecacarbonyltetrairidium In various solvent(s) at 175℃; under 760 Torr; Further byproducts given;A 1%
B 17%
C 56%
D 11%
n-heptane
142-82-5

n-heptane

A

2-Methylhexane
591-76-4

2-Methylhexane

B

3-methyl-hexane
589-34-4

3-methyl-hexane

C

Isobutane
75-28-5

Isobutane

D

methylbutane
78-78-4

methylbutane

Conditions
ConditionsYield
With aluminum oxide; silica gel; boron trichloride at 59.85℃; Product distribution;A n/a
B n/a
C 13%
D 55%
2,4,6-tri-t-butylphenyl-fluoro-(phenylamino)borane
152240-86-3

2,4,6-tri-t-butylphenyl-fluoro-(phenylamino)borane

A

2,4,6-tri-t-butylphenyl-(phenylimino)borane
152240-89-6

2,4,6-tri-t-butylphenyl-(phenylimino)borane

B

Isobutane
75-28-5

Isobutane

Conditions
ConditionsYield
With tert.-butyl lithium In hexane byproducts: LiF; dropping a soln. of t-butyl lithium in n-hexane to a soln. of 2,4,6-tri-t-butylphenyl-fluoro-(phenylamino)borane in n-hexane under N2 at -20°C and allowing to stand overnight; removal of the solvent under reduced pressure and subliming the iminoborane from the residue in an oil pump vacuum, elem. anal.;A 54%
B n/a
Isobutane
75-28-5

Isobutane

A

acetone
67-64-1

acetone

B

tert-butyl alcohol
75-65-0

tert-butyl alcohol

Conditions
ConditionsYield
With N-hydroxyphthalimide; air; cobalt acetylacetonate In benzonitrile at 100℃; under 7600 Torr; for 8h; Oxidation;A 13%
B 84%
With oxygen; azido(tetraphenylporphyrinato) complex of Cr(III) In benzene at 80℃; under 5171.5 Torr; for 6h;A 0.8 mmol
B 6.3 mmol
3-bromo-9H-carbazole
1592-95-6

3-bromo-9H-carbazole

Isobutane
75-28-5

Isobutane

C15H16BNO2

C15H16BNO2

Conditions
ConditionsYield
With copper(l) iodide; caesium carbonate; ethylenediamine In toluene Reflux;83%
Isobutane
75-28-5

Isobutane

A

acetone
67-64-1

acetone

B

isobutene
115-11-7

isobutene

Conditions
ConditionsYield
With oxygen Rate constant; Product distribution; var. oxygen pressure; time dependence;A 20%
B 80%
Isobutane
75-28-5

Isobutane

methyl-d3-propane-1,1,1,3,3,3-d6
13275-39-3

methyl-d3-propane-1,1,1,3,3,3-d6

Conditions
ConditionsYield
With DUSY zeolite at 200℃; Substitution;80%
perfluoropropylene
116-15-4

perfluoropropylene

Isobutane
75-28-5

Isobutane

A

4,4-Dimethyl-1,1,1,2,3,3-hexafluoropentane
53005-29-1

4,4-Dimethyl-1,1,1,2,3,3-hexafluoropentane

B

1,1,1,2,3,3-Hexafluoro-5-methylhexane

1,1,1,2,3,3-Hexafluoro-5-methylhexane

Conditions
ConditionsYield
With di-tert-butyl peroxide at 140℃; for 24h; Product distribution; Further Variations:; Reagents; Temperatures; time; irradiation; Addition;A 80%
B 3%
Isobutane
75-28-5

Isobutane

tertiary butyl chloride
507-20-0

tertiary butyl chloride

Conditions
ConditionsYield
With dichloromethane; antimony pentafluoride 1.) -78 deg C, 2 h, 2.) RT, 24 h;76%
at -15℃; Photochlorierung;
at 54℃; bei der photochemischen Chlorierung;
at 450 - 500℃; bei der thermischen Chlorierung;
Isobutane
75-28-5

Isobutane

diethyl 2-(ethoxycarbonylmethylene)malonate
13049-86-0

diethyl 2-(ethoxycarbonylmethylene)malonate

C15H26O6

C15H26O6

Conditions
ConditionsYield
With tetrakis(tetrabutylammonium)decatungstate(VI) In water; acetonitrile at 20℃; under 7500.75 Torr; for 4h; UV-irradiation; Flow reactor;76%
Isobutane
75-28-5

Isobutane

t-butyl bromide
507-19-7

t-butyl bromide

Conditions
ConditionsYield
With antimony pentafluoride; 1,2-dibromomethane 1.) -78 deg C, 2 h, 2.) RT, 24 h;75%
With bromine
With bromine
With bromine
Isobutane
75-28-5

Isobutane

ammonia
7664-41-7

ammonia

hydrogen cyanide
74-90-8

hydrogen cyanide

Conditions
ConditionsYield
oxyhydrogen flame; ratio of i-C4H10/NH3 = 1.07;71.8%
Isobutane
75-28-5

Isobutane

3-methylenebicyclo[2.2.1]heptan-2-one
5597-27-3

3-methylenebicyclo[2.2.1]heptan-2-one

C12H20O

C12H20O

Conditions
ConditionsYield
With tetrakis(tetrabutylammonium)decatungstate(VI) In water; acetonitrile at 20℃; under 7500.75 Torr; for 4h; UV-irradiation; Flow reactor;71%
Isobutane
75-28-5

Isobutane

Acetyl bromide; compound with GENERIC INORGANIC NEUTRAL COMPONENT

Acetyl bromide; compound with GENERIC INORGANIC NEUTRAL COMPONENT

benzene
71-43-2

benzene

A

4'-t-butylacetophenone
943-27-1

4'-t-butylacetophenone

B

acetophenone
98-86-2

acetophenone

Conditions
ConditionsYield
In dichloromethane Product distribution; 1.) -30 deg C, 2.) 17-19 deg C; other alkanes and cycloalkanes and aprotic superacids, also bromobenzene, var. temp. and time;A 68%
B 35%

75-28-5Relevant articles and documents

Rational Preparation of Well-Defined Multinuclear Iridium-Aluminum Polyhydride Clusters and Comparative Reactivity

Camp, Clément,Del Rosal, Iker,Escomel, Léon,Jeanneau, Erwann,Maron, Laurent,Robin, Emmanuel,Soulé, Na?me,Thieuleux, Chloé

, (2022/02/10)

We report an original alkane elimination approach, entailing the protonolysis of triisobutylaluminum by the acidic hydrides from Cp*IrH4. This strategy allows access to a series of well-defined tri- and tetranuclear iridium aluminum polyhydride clusters, depending on the stoichiometry: [Cp*IrH3Al(iBu)2]2(1), [Cp*IrH2Al(iBu)]2(2), [(Cp*IrH3)2Al(iBu)] (3), and [(Cp*IrH3)3Al] (4). Contrary to most transition-metal aluminohydride complexes, which can be considered as [AlHx+3]x-aluminates and LnM+moieties, the situation here is reversed: These complexes have original structures that are best described as [Cp*IrHx]n-iridate units surrounding cationic Al(III) fragments. This is corroborated by reactivity studies, which show that the hydrides are always retained at the iridium sites and that the [Cp*IrH3]-moieties are labile and can be transmetalated to yield potassium ([KIrCp*H3], 8) or silver (([AgIrCp*H3]n, 10) derivatives of potential synthetic interest. DFT calculations show that the bonding situation can vary in these systems, from 3-center 2-electron hydride-bridged Lewis adducts of the form Ir-H←Al to direct polarized metal-metal interaction from donation of d-electrons of Ir to the Al metal, and both types of interactions take place to some extent in each of these clusters.

Hydrogenative metathesis of enynes via piano-stool ruthenium carbene complexes formed by alkyne gem-hydrogenation

Peil, Sebastian,Bistoni, Giovanni,Goddard, Richard,Fürstner, Alois

supporting information, p. 18541 - 18553 (2020/11/17)

The only recently discovered gem-hydrogenation of internal alkynes is a fundamentally new transformation, in which both H atoms of dihydrogen are transferred to the same C atom of a triple bond while the other position transforms into a discrete metal carbene complex. [Cp?RuCl]4 is presently the catalyst of choice: the resulting piano-stool ruthenium carbenes can engage a tethered alkene into either cyclopropanation or metathesis, and a prototypical example of such a reactive intermediate with an olefin ligated to the ruthenium center has been isolated and characterized by X-ray diffraction. It is the substitution pattern of the olefin that determines whether metathesis or cyclopropanation takes place: a systematic survey using alkenes of largely different character in combination with a computational study of the mechanism at the local coupled cluster level of theory allowed the preparative results to be sorted and an intuitive model with predictive power to be proposed. This model links the course of the reaction to the polarization of the double bond as well as to the stability of the secondary carbene complex formed, if metathesis were to take place. The first application of "hydrogenative metathesis"to the total synthesis of sinularones E and F concurred with this interpretation and allowed the proposed structure of these marine natural products to be confirmed. During this synthesis, it was found that gem-hydrogenation also provides opportunities for C-H functionalization. Moreover, silylated alkynes are shown to participate well in hydrogenative metathesis, which opens a new entry into valuable allylsilane building blocks. Crystallographic evidence suggests that the polarized [Ru-Cl] bond of the catalyst interacts with the neighboring R3Si group. Since attractive interligand Cl/R3Si contacts had already previously been invoked to explain the outcome of various ruthenium-catalyzed reactions, including trans-hydrosilylation, the experimental confirmation provided herein has implications beyond the present case.

Decarbonylative ether dissection by iridium pincer complexes

Yoo, Changho,Dodge, Henry M.,Farquhar, Alexandra H.,Gardner, Kristen E.,Miller, Alexander J.M.

, p. 12130 - 12138 (2020/11/26)

A unique chain-rupturing transformation that converts an ether functionality into two hydrocarbyl units and carbon monoxide is reported, mediated by iridium(i) complexes supported by aminophenylphosphinite (NCOP) pincer ligands. The decarbonylation, which involves the cleavage of one C-C bond, one C-O bond, and two C-H bonds, along with formation of two new C-H bonds, was serendipitously discovered upon dehydrochlorination of an iridium(iii) complex containing an aza-18-crown-6 ether macrocycle. Intramolecular cleavage of macrocyclic and acyclic ethers was also found in analogous complexes featuring aza-15-crown-5 ether or bis(2-methoxyethyl)amino groups. Intermolecular decarbonylation of cyclic and linear ethers was observed when diethylaminophenylphosphinite iridium(i) dinitrogen or norbornene complexes were employed. Mechanistic studies reveal the nature of key intermediates along a pathway involving initial iridium(i)-mediated double C-H bond activation. This journal is

Synthesis and catalytic performance of zeolite-Y supported on silicon carbide in n-heptane cracking

Alhassan, Saeed M.,Berthod, Mikael,Dabbawala, Aasif A.,Joseph, Tony,Khan, Shaihroz,Mittal, Hemant,Morin, Stephane,Singaravel, Gnana,Vaithilingam, Balasubramanian V.,Wahedi, Yasser Al

, (2020/10/27)

In this work, we demonstrate a facile approach for the synthesis of zeolite-Y crystals (size, ca. ~400 nm) supported on silicon carbide (SiC) with the assistance of the cationic template (polydiallyldimethylammonium chloride, PDDA). The polymeric cationic template used to treat SiC particles induces a positive charge on SiC surface which electrostatically attracts negatively charged aluminosilicate seeds and promotes the growth of zeolite (ZY) particles over SiC, thus leading to the formation of stable ZY?SiC supported catalysts. The supported ZY catalysts with different weight ratio of ZY and SiC were synthesized and characterized by various techniques such as XRD, SEM, SEM-EDX, SEM-mapping, TEM, STEM, FT-IR, 27Al MAS NMR and N2 sorption. The characterization of the supported ZY catalysts suggests the uniform growth of ZY particles over SiC together with the creation of hierarchical micro-mesopores assembly. In the catalytic cracking of n-heptane, the catalyst ZY?SiC-50 displayed a remarkable improvement in reaction rate when compared to commercial zeolite-Y (CBV-600) amounting to 3.5 folds enhancement. Interestingly, the light olefins yield is also substantially improved. At WHSV of 8 h?1 and 475 °C, the highest light olefin yield (24–36 %) was achieved over ZY?SiC-50 whereas the reference catalyst, CBV-600 produced lower light olefins yield (7–17 %). Moreover, the supported ZY catalyst exhibited less deactivation rates. This improved performance is attributed to the hierarchical micro-mesopores assembly created by the homogeneous dispersion of zeolite crystals on SiC which offers fast diffusion pathways for the reactants and enhanced accessibility to active sites thus leading to higher observed reaction rates and fast diffusion of products thus minimizing the occurrence of side reactions.

PREPARATION METHOD FOR PREPARING A CATALYST BASED ON IRON NANOPARTICLES, COBALT NANOPARTICLES OR ALLOYS THEREOF, THE CATALYST THUS PREPARED AND USE OF THE CATALYST FOR THE SELECTIVE HYDROGENATION OF CARBON DIOXIDE TO ISOBUTANE

-

Page/Page column 14-15; 17-18, (2020/06/19)

The present invention describes a preparation method for preparing a catalyst made up of a Fe and Co metal alloy in several ratios in the form of nanoparticles embedded in a graphitic carbon matrix. Another object of the invention is also the prepared catalyst which in a surprising manner selectively catalyses the hydrogenation of carbon dioxide into isobutane.

Impact of the Spatial Organization of Bifunctional Metal–Zeolite Catalysts on the Hydroisomerization of Light Alkanes

Cheng, Kang,Harmel, Justine,Oenema, Jogchum,Sunley, Glenn,Yoshida, Hideto,Ze?evi?, Jovana,Zhang, Zhaorong,de Jong, Krijn P.,van der Wal, Lars I.

supporting information, p. 3592 - 3600 (2020/02/05)

Improving product selectivity by controlling the spatial organization of functional sites at the nanoscale is a critical challenge in bifunctional catalysis. We present a series of composite bifunctional catalysts consisting of one-dimensional zeolites (ZSM-22 and mordenite) and a γ-alumina binder, with platinum particles controllably deposited either on the alumina binder or inside the zeolite crystals. The hydroisomerization of n-heptane demonstrates that the catalysts with platinum particles on the binder, which separates platinum and acid sites at the nanoscale, leads to a higher yield of desired isomers than catalysts with platinum particles inside the zeolite crystals. Platinum particles within the zeolite crystals impose pronounced diffusion limitations on reaction intermediates, which leads to secondary cracking reactions, especially for catalysts with narrow micropores or large zeolite crystals. These findings extend the understanding of the ??intimacy criterion” for the rational design of bifunctional catalysts for the conversion of low-molecular-weight reactants.

Room Temperature Acceptorless Alkane Dehydrogenation from Molecular σ-Alkane Complexes

McKay, Alasdair I.,Bukvic, Alexander J.,Tegner, Bengt E.,Burnage, Arron L.,Mart?nez-Mart?nez, Antonio J.,Rees, Nicholas H.,Macgregor, Stuart A.,Weller, Andrew S.

supporting information, p. 11700 - 11712 (2019/08/20)

The non-oxidative catalytic dehydrogenation of light alkanes via C-H activation is a highly endothermic process that generally requires high temperatures and/or a sacrificial hydrogen acceptor to overcome unfavorable thermodynamics. This is complicated by alkanes being such poor ligands, meaning that binding at metal centers prior to C-H activation is disfavored. We demonstrate that by biasing the pre-equilibrium of alkane binding, by using solid-state molecular organometallic chemistry (SMOM-chem), well-defined isobutane and cyclohexane σ-complexes, [Rh(Cy2PCH2CH2PCy2)(η: η-(H3C)CH(CH3)2][BArF4] and [Rh(Cy2PCH2CH2PCy2)(η: η-C6H12)][BArF4] can be prepared by simple hydrogenation in a solid/gas single-crystal to single-crystal transformation of precursor alkene complexes. Solid-gas H/D exchange with D2 occurs at all C-H bonds in both alkane complexes, pointing to a variety of low energy fluxional processes that occur for the bound alkane ligands in the solid-state. These are probed by variable temperature solid-state nuclear magnetic resonance experiments and periodic density functional theory (DFT) calculations. These alkane σ-complexes undergo spontaneous acceptorless dehydrogenation at 298 K to reform the corresponding isobutene and cyclohexadiene complexes, by simple application of vacuum or Ar-flow to remove H2. These processes can be followed temporally, and modeled using classical chemical, or Johnson-Mehl-Avrami-Kologoromov, kinetics. When per-deuteration is coupled with dehydrogenation of cyclohexane to cyclohexadiene, this allows for two successive KIEs to be determined [kH/kD = 3.6(5) and 10.8(6)], showing that the rate-determining steps involve C-H activation. Periodic DFT calculations predict overall barriers of 20.6 and 24.4 kcal/mol for the two dehydrogenation steps, in good agreement with the values determined experimentally. The calculations also identify significant C-H bond elongation in both rate-limiting transition states and suggest that the large kH/kD for the second dehydrogenation results from a pre-equilibrium involving C-H oxidative cleavage and a subsequent rate-limiting β-H transfer step.

Hydrogen Activation and Hydrogenolysis Facilitated by Late-Transition-Metal-Aluminum Heterobimetallic Complexes

Charles, R. Malcolm,Yokley, Timothy W.,Schley, Nathan D.,Deyonker, Nathan J.,Brewster, Timothy P.

, p. 12635 - 12645 (2019/10/11)

Previously reported heterobimetallic rhodium-aluminum and iridium-aluminum alkyl complexes are shown to activate hydrogen, generating the corresponding alkane. Kinetic data indicate a mechanistic difference between the iridium- A nd rhodium-based systems. In both cases the transition metal is an active participant in the release of alkane from the aluminum center. For iridium-aluminum species, experimental mechanistic data suggest that multiple pathways occur concomitantly with each other: One being the oxidative addition of hydrogen followed by proton transfer resulting in alkane generation. Computational data indicate a reasonable barrier to formation of an iridium dihydride intermediate observed experimentally. In the case of the rhodium-aluminum species, hydrides are not observed spectroscopically, though a reasonable barrier to formation of this thermodynamically unstable species has been calculated. Alternative mechanistic possibilities are discussed and explored computationally. Cooperative hydrogenolysis mechanisms are computed to be energetically unfeasible for both metal centers.

Hydrocarbon Synthesis via Photoenzymatic Decarboxylation of Carboxylic Acids

Zhang, Wuyuan,Ma, Ming,Huijbers, Mieke M. E.,Filonenko, Georgy A.,Pidko, Evgeny A.,Van Schie, Morten,De Boer, Sabrina,Burek, Bastien O.,Bloh, Jonathan Z.,Van Berkel, Willem J. H.,Smith, Wilson A.,Hollmann, Frank

supporting information, p. 3116 - 3120 (2019/03/06)

A recently discovered photodecarboxylase from Chlorella variabilis NC64A (CvFAP) bears the promise for the efficient and selective synthesis of hydrocarbons from carboxylic acids. CvFAP, however, exhibits a clear preference for long-chain fatty acids thereby limiting its broad applicability. In this contribution, we demonstrate that the decoy molecule approach enables conversion of a broad range of carboxylic acids by filling up the vacant substrate access channel of the photodecarboxylase. These results not only demonstrate a practical application of a unique, photoactivated enzyme but also pave the way to selective production of short-chain alkanes from waste carboxylic acids under mild reaction conditions.

Hydrogenation of CO2 into aromatics over a ZnCrO: X-zeolite composite catalyst

Zhang, Junfeng,Zhang, Meng,Chen, Shuyao,Wang, Xiaoxing,Zhou, Zeling,Wu, Yingquan,Zhang, Tao,Yang, Guohui,Han, Yizhuo,Tan, Yisheng

supporting information, p. 973 - 976 (2019/01/23)

A ZnCrOx-ZnZSM-5 composite catalyst was used for CO2 hydrogenation into hydrocarbons especially aromatics (Aro). 81.1% Aro selectivity in C5+ hydrocarbons (mainly C5-11) was obtained at 320 °C, corresponding to 19.9% CO2 conversion, 29.8% total hydrocarbons (HCt) selectivity and 69.7% C5+ selectivity in HCt. Our optimized STY of Aro is the highest ever reported.

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