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Propane, also known as LPG (liquefied petroleum gas), is a colorless, odorless gas that is primarily used as a fuel for heating, cooking, and various other applications. It is a byproduct of natural gas processing and petroleum refining, and is also produced during the refining of crude oil. Propane is highly flammable and is stored in pressurized tanks as a liquid, but it vaporizes into a gas when released. It is a clean-burning fuel that produces minimal emissions, making it an environmentally friendly choice for many applications. Propane is a versatile and efficient energy source that is widely available and relatively inexpensive.

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  • 74-98-6 Structure
  • Basic information

    1. Product Name: Propane
    2. Synonyms: n-Propane;Dimethylmethane;HC 290;LPG;Liquefied petroleum gas;Propyl hydride;Purifrigor P 2;Purifrigor P 3;R 280;
    3. CAS NO:74-98-6
    4. Molecular Formula: C3H8
    5. Molecular Weight: 44.11
    6. EINECS: 200-827-9
    7. Product Categories: N/A
    8. Mol File: 74-98-6.mol
  • Chemical Properties

    1. Melting Point: N/A
    2. Boiling Point: -42.1 °C
    3. Flash Point: -104 °C
    4. Appearance: colourless odourless gas
    5. Density: 0.565 g/cm3
    6. Refractive Index: N/A
    7. Storage Temp.: N/A
    8. Solubility: N/A
    9. CAS DataBase Reference: Propane(CAS DataBase Reference)
    10. NIST Chemistry Reference: Propane(74-98-6)
    11. EPA Substance Registry System: Propane(74-98-6)
  • Safety Data

    1. Hazard Codes: N/A
    2. Statements: N/A
    3. Safety Statements: N/A
    4. RIDADR: 1978
    5. WGK Germany:
    6. RTECS:
    7. HazardClass: 2.1
    8. PackingGroup: N/A
    9. Hazardous Substances Data: 74-98-6(Hazardous Substances Data)

74-98-6 Usage

Uses

Used in Residential Applications:
Propane is used as a fuel for heating and cooking in residential settings, providing a clean and efficient energy source for homes.
Used in Commercial Applications:
In the commercial sector, propane is used for various purposes, including heating, cooking, and powering equipment such as forklifts and generators.
Used in Industrial Applications:
Propane is utilized in the industrial sector for processes like welding, cutting, and powering heavy machinery.
Used in Automotive Applications:
Propane is used as an alternative fuel for vehicles, offering a cleaner and more environmentally friendly option compared to traditional gasoline or diesel fuels.
Used in Agricultural Applications:
In agriculture, propane is employed for various purposes, such as powering irrigation pumps, drying crops, and providing heat for greenhouses.
Used in Recreational Applications:
Propane is commonly used in recreational vehicles (RVs) and boats as a fuel source for heating, cooking, and other onboard needs.
Used in Emergency Power Applications:
Propane-powered generators are used as backup power sources during power outages, providing a reliable and clean energy option for emergency situations.

Check Digit Verification of cas no

The CAS Registry Mumber 74-98-6 includes 5 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 2 digits, 7 and 4 respectively; the second part has 2 digits, 9 and 8 respectively.
Calculate Digit Verification of CAS Registry Number 74-98:
(4*7)+(3*4)+(2*9)+(1*8)=66
66 % 10 = 6
So 74-98-6 is a valid CAS Registry Number.
InChI:InChI=1/C3H8/c1-3-2/h3H2,1-2H3

74-98-6 Well-known Company Product Price

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  • Aldrich

  • (536172)  Propane  99.97%

  • 74-98-6

  • 536172-145G

  • 3,997.89CNY

  • Detail
  • Aldrich

  • (769037)  Propane  99.95%, Messer® CANGas

  • 74-98-6

  • 769037-1L

  • 947.70CNY

  • Detail

74-98-6SDS

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 propane

1.2 Other means of identification

Product number -
Other names Lpg

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:74-98-6 SDS

74-98-6Synthetic route

propene
187737-37-7

propene

propane
74-98-6

propane

Conditions
ConditionsYield
With para-hydrogen under 5414.51 Torr; Flow reactor;100%
With hydrogen; nickel at 40℃; Thermodynamic data; Ea, various catalysts;
With hydrogen at 151.9 - 326.9℃; under 100 Torr; Kinetics; Ir(1.1.1)-surface; pc-C3H6 2.0 torr; kapp0, Eapp;
carbon monoxide
201230-82-2

carbon monoxide

A

methane
34557-54-5

methane

B

ethane
74-84-0

ethane

C

propane
74-98-6

propane

D

carbon dioxide
124-38-9

carbon dioxide

E

water

water

Conditions
ConditionsYield
With hydrogen; nickel at 329.9℃; nickel powder, prepared by evaporation-condensation; Yields of byproduct given;A 98%
B n/a
C n/a
D n/a
E n/a
propene
187737-37-7

propene

Triethoxysilane
998-30-1

Triethoxysilane

A

propane
74-98-6

propane

B

allyltriethoxysilane
2550-04-1

allyltriethoxysilane

Conditions
ConditionsYield
With DIP-Co catalysts at 23℃; Reagent/catalyst; Inert atmosphere; Glovebox;A n/a
B 98%
tris(cyclopentadienyl)thoriumisopropyl

tris(cyclopentadienyl)thoriumisopropyl

A

propene
187737-37-7

propene

B

propane
74-98-6

propane

Conditions
ConditionsYield
In benzene-d6 Kinetics; thermolysis at 167 +/- 1°C;A <2
B 97%
In benzene Irradiation (UV/VIS); photolysis in a frozen benzene soln.;
tetrachloromethane
56-23-5

tetrachloromethane

di-n-propylmercury
628-85-3

di-n-propylmercury

A

propene
187737-37-7

propene

B

propane
74-98-6

propane

C

mercury

mercury

Conditions
ConditionsYield
In neat (no solvent) 150°C, 60 h; further products;A 91%
B 5%
C 95%
tetrachloromethane
56-23-5

tetrachloromethane

oxygen
80937-33-3

oxygen

diisopropylmercury
1071-39-2

diisopropylmercury

A

propane
74-98-6

propane

B

isopropyl chloride
75-29-6

isopropyl chloride

C

chloroform
67-66-3

chloroform

D

isopropylmercury(II) chloride
30615-19-1

isopropylmercury(II) chloride

E

mercury

mercury

Conditions
ConditionsYield
In neat (no solvent) 20°C, 96 h; further products;A 4%
B 48%
C 30%
D 95%
E 5%
triethylsilane
617-86-7

triethylsilane

2-butyl ethyl ether
625-54-7

2-butyl ethyl ether

A

propane
74-98-6

propane

B

ethoxytriethylsilane
597-67-1

ethoxytriethylsilane

Conditions
ConditionsYield
nickel at 100 - 120℃; for 1h;A n/a
B 90%
triethylsilane
617-86-7

triethylsilane

butyl isopropyl ether
1860-27-1

butyl isopropyl ether

A

propane
74-98-6

propane

B

n-butoxytriethylsilane
2751-87-3

n-butoxytriethylsilane

Conditions
ConditionsYield
nickel at 100 - 120℃; for 1h;A n/a
B 90%
isopropyl bromide
75-26-3

isopropyl bromide

propane
74-98-6

propane

Conditions
ConditionsYield
With triethylamine In water at 20℃; for 2h; Inert atmosphere; Irradiation;90%
Co(BF4)2(bipy)n Product distribution; Electrochemical reaction;
lanthanum dicarbide

lanthanum dicarbide

water
7732-18-5

water

A

methane
34557-54-5

methane

B

ethane
74-84-0

ethane

C

propane
74-98-6

propane

D

ethene
74-85-1

ethene

E

acetylene
74-86-2

acetylene

Conditions
ConditionsYield
In neat (no solvent) hydrolysis in water vapor (11.0E2 Nm**2);A 0.24%
B 6.77%
C 0.14%
D 2.54%
E 89.5%
tris(η3-allyl)chromium
27303-69-1

tris(η3-allyl)chromium

A

propane
74-98-6

propane

B

chromium
7440-47-3

chromium

Conditions
ConditionsYield
With hydrogen In further solvent(s) High Pressure; in perhydrocumol at 100 at;;A 89%
B n/a
With H2 In further solvent(s) High Pressure; in perhydrocumol at 100 at;;A 89%
B n/a
(PPh3)3CoH(N2)
21373-88-6, 16920-54-0

(PPh3)3CoH(N2)

phenyl butanoate
4346-18-3

phenyl butanoate

A

HCo(CO)(P(C6H5)3)3
53729-69-4, 21329-67-9

HCo(CO)(P(C6H5)3)3

B

phenoxotris(triphenylphosphine)cobalt(I)
91583-66-3

phenoxotris(triphenylphosphine)cobalt(I)

C

propane
74-98-6

propane

D

butyl butyrate
109-21-7

butyl butyrate

E

nitrogen
7727-37-9

nitrogen

Conditions
ConditionsYield
In toluene byproducts: H2; n-PrCO2Ph added to CoH(N2)(PPh3)3 in toluene in vac., reacted for 1 day at room temp.; liquid phase analysed by GLC; hexane added, ppt. filtered, washed with hexane, dried in vac., recrystd. from C6H6-hexane;A n/a
B 60%
C 12%
D 38%
E 89%
methanol
67-56-1

methanol

A

propene
187737-37-7

propene

B

methane
34557-54-5

methane

C

ethane
74-84-0

ethane

D

propane
74-98-6

propane

E

ethene
74-85-1

ethene

F

n-butane
106-97-8

n-butane

Conditions
ConditionsYield
Ni-SAPO-34 at 450℃; under 760 Torr; for 1h; Product distribution; var. temp.;A 5.26%
B 1.5%
C 1.02%
D 0.15%
E 88.04%
F 0.03%
molecular sieve In gas at 300℃; Product distribution; other temperatures; other products;
With hydrogen; proton-type ZSM-5 at 330℃; under 1050.11 Torr; Product distribution / selectivity; Gas phase;
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;
glycerol
56-81-5

glycerol

A

propan-1-ol
71-23-8

propan-1-ol

B

propane
74-98-6

propane

Conditions
ConditionsYield
With hydrogen In 1,4-dioxane at 159.84℃; under 60006 Torr; for 24h; Autoclave;A 87%
B 9%
With [Ru(OH2)3(4'-phenyl-2,2':6',2''-terpy)](OTf)2; hydrogen; ortho-tungstic acid In water at 250℃; under 41254.1 Torr; for 24h;A 39 %Chromat.
B 52 %Chromat.
With hydrogen In water at 200℃; under 18751.9 Torr; for 16h; Autoclave;
{1,2-bis(diphenylphosphino)ethane}(butane-1,4-diyl)palladium

{1,2-bis(diphenylphosphino)ethane}(butane-1,4-diyl)palladium

A

1-butylene
106-98-9

1-butylene

B

(Z)-2-Butene
590-18-1

(Z)-2-Butene

C

trans-2-Butene
624-64-6

trans-2-Butene

D

propane
74-98-6

propane

E

ethene
74-85-1

ethene

Conditions
ConditionsYield
In toluene thermal decompn. at 60°C (15 h); further product: cyclobutane;A 85.9%
B 3.4%
C 3.6%
D 1%
E 5.7%
In toluene thermal decompn. at 95°C (15 h); further product: cyclobutane;A 58.7%
B 2.5%
C 2.5%
D 1%
E 36.3%
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%
allyl alcohol
107-18-6

allyl alcohol

A

propene
187737-37-7

propene

B

propane
74-98-6

propane

Conditions
ConditionsYield
With methanol; toluene-4-sulfonic acid at 25℃; for 12h; Time; Sealed tube; Inert atmosphere; UV-irradiation;A 85%
B 11%
With methanol; 5% Pd/TiO2; toluene-4-sulfonic acid at 25℃; for 12h; Inert atmosphere; UV-irradiation;
carbon monoxide
201230-82-2

carbon monoxide

A

propene
187737-37-7

propene

B

methane
34557-54-5

methane

C

ethane
74-84-0

ethane

D

propane
74-98-6

propane

Conditions
ConditionsYield
With hydrogen; nickel at 473℃; under 159.8 Torr;A 8%
B 84%
C 4%
D 4%
With hydrogen; cobalt-manganese oxide at 190℃; under 4500.4 Torr; Further byproducts given. Yields of byproduct given;
With hydrogen; TiC Yield given. Further byproducts given. Yields of byproduct given. Title compound not separated from byproducts;
n-butane
106-97-8

n-butane

A

propene
187737-37-7

propene

B

methane
34557-54-5

methane

C

ethane
74-84-0

ethane

D

propane
74-98-6

propane

E

ethene
74-85-1

ethene

Conditions
ConditionsYield
at 570 - 630℃; Kinetics;A 68%
B 83%
C 20%
D 4%
E 30%
ferrerite zeolite at 650℃;
butanoic acid anhydride
106-31-0

butanoic acid anhydride

(PPh3)3CoH(N2)
21373-88-6, 16920-54-0

(PPh3)3CoH(N2)

A

Co(OCO-n-C3H7)
99668-71-0

Co(OCO-n-C3H7)

B

propane
74-98-6

propane

C

butyl butyrate
109-21-7

butyl butyrate

D

nitrogen
7727-37-9

nitrogen

E

hydrogen
1333-74-0

hydrogen

Conditions
ConditionsYield
In toluene in toluene at room temp. for 1 day;A n/a
B 16%
C 30%
D 81%
E 13%
ethyl bromide
74-96-4

ethyl bromide

dimethylnickel{1,2-bis(diphenylphosphino)ethane}
31387-22-1

dimethylnickel{1,2-bis(diphenylphosphino)ethane}

A

dibromo[1,2-bis(diphenylphosphino)ethane]nickel(II)
14647-21-3

dibromo[1,2-bis(diphenylphosphino)ethane]nickel(II)

B

methane
34557-54-5

methane

C

ethane
74-84-0

ethane

D

propane
74-98-6

propane

E

ethene
74-85-1

ethene

Conditions
ConditionsYield
In toluene EtBr added into toluene soln. of Ni complex, stirred at 35°C for48 h; evapd. in vac., crystd. from Et2O-hexane; GLC anal.;A 48%
B 78%
C 70%
D 10%
E 33%
chloroform
67-66-3

chloroform

ethylmagnesium chloride
2386-64-3

ethylmagnesium chloride

A

propane
74-98-6

propane

B

3-ethylpentane
617-78-7

3-ethylpentane

C

pentane
109-66-0

pentane

Conditions
ConditionsYield
With C31H37ClN3NiO2(1-)*Li(1+) In tetrahydrofuran at 25℃; for 0.333333h; Inert atmosphere; Overall yield = 93.4 %;A 6%
B 9.4%
C 78%
With C31H37ClFeN3O2 In tetrahydrofuran at 25℃; for 0.0833333h; Inert atmosphere;
butanoic acid anhydride
106-31-0

butanoic acid anhydride

(PPh3)3CoCH3

(PPh3)3CoCH3

A

Co(OCO-n-C3H7)
99668-71-0

Co(OCO-n-C3H7)

B

propene
187737-37-7

propene

C

methane
34557-54-5

methane

D

propane
74-98-6

propane

E

2-Pentanone
107-87-9

2-Pentanone

Conditions
ConditionsYield
In tetrahydrofuran in THF at -40-20°C;A n/a
B 7%
C 6%
D 2%
E 76%
carbon monoxide
201230-82-2

carbon monoxide

A

methane
34557-54-5

methane

B

ethane
74-84-0

ethane

C

propane
74-98-6

propane

Conditions
ConditionsYield
With hydrogen; Ni-B(P-1) at 473℃; under 159.8 Torr;A 75%
B 17%
C 8%
With hydrogen; technetium at 240℃; Product distribution; Thermodynamic data; E(a); other supporting materials of the technetium catalyst; var. temperatures;A 81.0 % Chromat.
B 17.9 % Chromat.
C 1.1 % Chromat.
With hydrogen at 210.3℃; under 3723.56 Torr; Product distribution / selectivity;
cis-methyldiethyl(triphenylphosphine)gold(III)

cis-methyldiethyl(triphenylphosphine)gold(III)

A

methane
34557-54-5

methane

B

ethane
74-84-0

ethane

C

propane
74-98-6

propane

D

n-butane
106-97-8

n-butane

Conditions
ConditionsYield
With sulfuric acid In not given acidolysis with H2SO4 (residue not identified);A 74.5%
B 16.3%
C 21%
D 72.3%
methane
34557-54-5

methane

A

propane
74-98-6

propane

B

hydrogen
1333-74-0

hydrogen

Conditions
ConditionsYield
for 16h; Product distribution / selectivity; γ-Irradiation; 25 psig;A 74%
B n/a
allyl iodid
556-56-9

allyl iodid

ReH7*2P(C6H5)3=ReH7(P(C6H5)3)2
12103-40-1

ReH7*2P(C6H5)3=ReH7(P(C6H5)3)2

A

propane
74-98-6

propane

B

2(C6H5)3PC3H5(1+)*ReI6(2-)=((C6H5)3PC3H5)2ReI6
85335-13-3

2(C6H5)3PC3H5(1+)*ReI6(2-)=((C6H5)3PC3H5)2ReI6

Conditions
ConditionsYield
In tetrahydrofuran byproducts: H2, propene; under N2, allyl iodide was reacted with Re-complex with stirring in THFat room temp. for 3 h; filtered, washed with THF and Et2O, recrystd. from CH2Cl2-THF; elem. anal.;A <1
B 74%
cis-methyldiethyl(triphenylphosphine)gold(III)

cis-methyldiethyl(triphenylphosphine)gold(III)

A

propane
74-98-6

propane

B

n-butane
106-97-8

n-butane

Conditions
ConditionsYield
In solid thermolysis at 110°C to propane, n-butane and an unidentified residue;A 22.3%
B 72.2%
trans-NiMe2(triethylphosphine)2
60542-85-0, 81131-93-3

trans-NiMe2(triethylphosphine)2

propyl bromide
106-94-5

propyl bromide

trans-dibromobis(triethylphosphine)nickel(II)
69460-30-6, 19224-77-2

trans-dibromobis(triethylphosphine)nickel(II)

B

propene
187737-37-7

propene

C

methane
34557-54-5

methane

D

ethane
74-84-0

ethane

E

propane
74-98-6

propane

Conditions
ConditionsYield
In toluene propyl bromide added into toluene soln. of NiMe2(PEt3)2, stirred at room temp. for 12 h; evapd. in vac., crystd. from Et2O-hexane; GLC anal.;A 71%
B 127 %
C 115 %
D 46%
E 35%
rhenium trioxide ion
34021-33-5

rhenium trioxide ion

propane
74-98-6

propane

rhenium dioxide propylene

rhenium dioxide propylene

Conditions
ConditionsYield
In gas byproducts: H2O; in gaseous phase; ion cyclotron resonance;100%
LaFe(1+)
111496-23-2

LaFe(1+)

propane
74-98-6

propane

A

LaFeC3H6(1+)

LaFeC3H6(1+)

B

hydrogen
1333-74-0

hydrogen

Conditions
ConditionsYield
In gas reaction in a mass spectrometer; sample pressure 4E-7 Torr;A 100%
B 100%
rhenium dioxide ion
71798-60-2

rhenium dioxide ion

propane
74-98-6

propane

rheniumoxopropylene

rheniumoxopropylene

Conditions
ConditionsYield
In gas byproducts: H2O; in gaseous phase; ion cyclotron resonance;100%
propane
74-98-6

propane

dirhenium ion
134161-52-7

dirhenium ion

dirhenium benzene ion

dirhenium benzene ion

Conditions
ConditionsYield
In gas in gaseous phase; ion cyclotron resonance;100%
propane
74-98-6

propane

carbon monoxide
201230-82-2

carbon monoxide

4-chlorophenyltrimethylsilane
10557-71-8

4-chlorophenyltrimethylsilane

1-(4-chlorophenyl)-2-methylpropan-1-one
18713-58-1

1-(4-chlorophenyl)-2-methylpropan-1-one

Conditions
ConditionsYield
With aluminum tri-bromide; carbon tetrabromide In various solvent(s) at 0℃; for 0.5h;97%
propane
74-98-6

propane

isopropyl bromide
75-26-3

isopropyl bromide

Conditions
ConditionsYield
With 2AlBr3*CBr4; bromine at -20℃; for 3h;96%
With antimony pentafluoride; 1,2-dibromomethane 1.) -78 deg C, 2 h, 2.) RT, 24 h;64%
With 2AlBr3*CBr4; bromine In various solvent(s) at -20℃; for 3h;48 % Turnov.
propane
74-98-6

propane

N-propyl-carbamic acid chloride
41891-16-1

N-propyl-carbamic acid chloride

Propyl isocyanate
110-78-1

Propyl isocyanate

Conditions
ConditionsYield
In 5,5-dimethyl-1,3-cyclohexadiene95%
propane
74-98-6

propane

[(η3-[2.1.1]-2,6-pyridinophane)Pt(IV)HMe2]B[3,5-(CF3)2C6H3]4
717139-15-6, 547695-25-0

[(η3-[2.1.1]-2,6-pyridinophane)Pt(IV)HMe2]B[3,5-(CF3)2C6H3]4

[Pt(η2-C3H6)H(η3-[2.1.1]-(2,6)-pyridinophane)] tetrakis[3,5-bis(trifluoromethyl)phenyl]borate
566200-10-0, 566933-21-9

[Pt(η2-C3H6)H(η3-[2.1.1]-(2,6)-pyridinophane)] tetrakis[3,5-bis(trifluoromethyl)phenyl]borate

Conditions
ConditionsYield
In dichloromethane Kinetics; byproducts: CH4; by a react. of propane (3 M) with Pt-contg. compd. at room temp. in CH2Cl2 soln. for 8 h; NMR studies; two diastereomers;95%
propane
74-98-6

propane

Pentafluorobenzene
363-72-4

Pentafluorobenzene

Pentafluor(isopropyl)benzol
52144-70-4

Pentafluor(isopropyl)benzol

Conditions
ConditionsYield
With aluminum tri-bromide; carbon tetrabromide In various solvent(s) at 0℃; for 1.5h;94%
With aluminum tri-bromide; carbon tetrabromide at 0℃; for 1.5h; Mechanism;
propane
74-98-6

propane

A

propene
187737-37-7

propene

B

methane
34557-54-5

methane

C

ethane
74-84-0

ethane

D

ethene
74-85-1

ethene

Conditions
ConditionsYield
With chromium(III) oxide; carbon dioxide at 549.9℃; Product distribution; other supporting materials for Cr2O3; also in the absence of CO2;A 91.3%
B 6.4%
C 0.7%
D 1.6%
at 500 - 600℃; Kinetics;A 46%
B 55%
C 7%
D 47%
With hydrogen-permeable palladium module and chromia-alumina catalyst (9.0 wt % Cr) at 550℃; Temperature;A 30%
B n/a
C n/a
D n/a
rhenium ion

rhenium ion

propane
74-98-6

propane

A

rhenium propylene ion

rhenium propylene ion

B

rhenium benzene ion
474654-47-2

rhenium benzene ion

Conditions
ConditionsYield
In gas in gaseous phase; ion cyclotron resonance;A 10%
B 90%
propene
187737-37-7

propene

ethane
74-84-0

ethane

propane
74-98-6

propane

acrylic acid
79-10-7

acrylic acid

Conditions
ConditionsYield
With oxygen; multimetal oxide catalyst at 274 - 316℃; Gas phase;86.1%
propene
187737-37-7

propene

propane
74-98-6

propane

ethene
74-85-1

ethene

acrylic acid
79-10-7

acrylic acid

Conditions
ConditionsYield
With oxygen; multimetal oxide catalyst at 274 - 316℃; Gas phase;86.1%

74-98-6Relevant articles and documents

Novel Rate Constants for a Catalytic Hydrogenation Reaction of Propylene Obtained by a Frequency Response Method

Yasuda, Yusuke,Iwai, Kayo,Takakura, Kazumi

, p. 17852 - 17861 (1995)

"Reaction rate (or FR) spectra" of a catalytic hydrogenation of propylene over Pt or Rh at 314 K were observed in a cell reactor composed of a proton-conducting membrane.It is shown that a variety of the spectra can be reproduced well by "characteristic functions", K*H(ω) and K*C(ω), which may be derived from a three-stage model composed of five elementary steps: X(g) -->/X(a) -->/X(a) --> propane (X: hydrogen or propylene), where X denotes the gaseous molecule; AX and BX are the first and second intermediate adsorbed species.Seven rate constants concerning these five steps were evaluated by matching K*H(ω) or K*C(ω) to the spectrum; five of them, kPX, k-AX, kAX, k-BX, and kBX, are ordinary rate constants, while the other two, l-BX and lBX, are novel ones.Since all these constants except kPX are independent of the amounts of catalyst, they are characteristic of active sites and can be compared with each other.On the basis of these constants, kinetic details have been discussed; for instance, mean residence times of AX and BX, τAX and τBX, respectively, were determined by (k-AX + kAX)-1 and (k-BX + kBX)-1, resulting in (in second units) τAH ca. 0.3 and τBH ca. 3 for hydrogen and τAC ca. 3 for propylene over Pt, while over Rh they were τAH ca. 1 and τBH ca. 3; τAC ca. 102 and τBC ca. 102.The nondimensional rate constants, l-BX and lBX, were indispensable to reproduce the various FR spectra; l-BH and lBH were positive, whereas l-BC and lBC were negative over both catalysts, which suggests heat effects.

Chemisorption and Surface Reactions in Cooperative Adsorption Systems.

Hesse

, p. 156 - 165 (1985)

The kinetics of propylene hydrogenation catalyzed by thermally treated supported platinum catalysts can be described by a Langmuir-Hinshelwood mechanism. The parameter values of the resulting rate equation, however, clearly depend on the coverage of the catalyst surface. Because of the instabilities observed with this reaction, it has to be assumed that lateral interaction of chemisorbed hydrogen and chemisorbed propylene is the main reason for this parameter variation. Using the lattice-gas model and the methods of statistical thermodynamics, straight-forward equations are derived which take into account the influence of this interaction on chemisorption and surface reaction in binary adsystems. The usefulness of these equations for the evaluation of kinetic measurements is demonstrated.

Frequency Response Method for the Study of Kinetics of a Heterogeneous Catalytic Reaction of Gases

Yasuda, Yusuke

, p. 7185 - 7190 (1989)

A new frequency response method is proposed on the basis of actual data on C3H6 + H2 -> C3H8 over Pt/Al2O3 at 273 K observed under each partial pressure of ca. 10 Pa: the gas space of a continuous-flow reactor was varied sinusoidally, and every partial pressure variation induced was followed by a mass spectrometer.Both amplitude and phase difference of ΔR observed in the angular frequency region from 40 to 60 rad/min were described well by , where Rs and PH(s) denote the overall reaction rate and the partial pressure of H2 at the steady state before the oscillation and is the time derivative of the pressure variation, dΔPH/dt.The "rate constant" n and κ were 0.15 and 7 * 1E-2 min, respectively.The unordinary rate equation involving PH was interpreted by R = ?dμd in terms of the driving force or the free energy drop, μd, and the frequency factor, ?d, at the rate-limiting step; Δ?d/?d = nΔPH/PH(s) and .The newly derived rate constant κ seemed to decrease with increasing temperature.The turnover frequency could be given by n/κ.

Organometallic complexes in supported ionic-liquid phase (SILP) catalysts: A PHIP NMR spectroscopy study

Gong, Qingxia,Klankermayer, Juergen,Bluemich, Bernhard

, p. 13795 - 13799 (2011)

para-Hydrogen induced polarization (PHIP) NMR spectroscopy emerges as an efficient and robust method for on-line monitoring of gas-phase hydrogenation reactions. Here we report detailed investigations of supported ionic liquid phase (SILP) catalysts in a continuous gas-phase hydrogenation of propene with PHIP NMR spectroscopy. A relocation of the rhodium complex in the thin layer of ionic liquid in the SILP catalyst at the initial stage of the propene hydrogenation is demonstrated. PHIP NMR spectroscopy can provide profound insight into the evolution of SILP catalysts during hydrogenation reactions.

Reductive dehalogenation of 1,3-dichloropropane by a [Ni(tetramethylcyclam)]Br2-Nafion modified electrode

Fontmorin,He,Floner,Fourcade,Amrane,Geneste

, p. 511 - 517 (2014)

Dechlorination reaction of 1,3-dichloropropane, a contaminant solvent, was investigated by electrochemical reduction in aqueous medium using a Ni(tmc)Br2complex, known as effective catalyst in dehalogenation reactions. The catalytic activity of the complex was first investigated by cyclic voltammetry and flow homogeneous redox catalysis using a graphite felt as working electrode. A total degradation of 1,3-dichloropropane was obtained after 5 h of electrolysis with a substrate/catalyst ratio of 2.3. The concentration of chloride ions determined by ion chromatography analysis showed a dechlorination yield of 98%. The complex was then immobilized on the graphite felt electrode in a Nafion film. Flow heterogeneous catalytic reduction of 1,3-dichloropropane was then carried out with the [Ni(tmc)]Br2-modified Nafion electrode. GC analyses underlined the total degradation of the substrate in only 3.5 h with a substrate/catalyst ratio of 100. A dechlorination yield of 80% was obtained, as seen with ion chromatography analyses of chloride ion. Comparison of both homogeneous and heterogeneous reactions highlighted the interest of the [Ni(tmc)]Br2-modified Nafion electrode that led to a higher stability of the catalyst with a turnover number of 180 and a higher current efficiency.

In situ x-ray absorption spectroscopy and nonclassical catalytic hydrogenation with an iron(II) catecholate immobilized on a porous organic polymer

Kraft, Steven J.,Hu, Bo,Zhang, Guanghui,Miller, Jeffrey T.,Hock, Adam S.

, p. 3972 - 3977 (2013)

The oxidation state and coordination number of immobilized iron catecholate EtO2Fe(CAT-POP) were determined by X-ray absorption spectroscopy (XAS) under a variety of conditions. We find the as-prepared material to be three-coordinate Fe2+ that readily oxidizes to Fe3+ upon exposure to air but remains three-coordinate. Both the reduced and oxidized Fe(CAT-POP) catalyze olefin hydrogenation in batch and flow reactors. We determined the catalytic rates for both species and also observed by means of XAS that the oxidation state of the iron centers does not change in hydrogen at the reaction temperature. Therefore, we postulate that the mechanism of hydrogenation by Fe(CAT-POP) proceeds through one of several possible nonclassical mechanisms, which are discussed.

Selective Catalytic Chemistry at Rhodium(II) Nodes in Bimetallic Metal–Organic Frameworks

Shakya, Deependra M.,Ejegbavwo, Otega A.,Rajeshkumar, Thayalan,Senanayake, Sanjaya D.,Brandt, Amy J.,Farzandh, Sharfa,Acharya, Narayan,Ebrahim, Amani M.,Frenkel, Anatoly I.,Rui, Ning,Tate, Gregory L.,Monnier, John R.,Vogiatzis, Konstantinos D.,Shustova, Natalia B.,Chen, Donna A.

, p. 16533 - 16537 (2019)

We report the first study of a gas-phase reaction catalyzed by highly dispersed sites at the metal nodes of a crystalline metal–organic framework (MOF). Specifically, CuRhBTC (BTC3?=benzenetricarboxylate) exhibited hydrogenation activity, while other isostructural monometallic and bimetallic MOFs did not. Our multi-technique characterization identifies the oxidation state of Rh in CuRhBTC as +2, which is a Rh oxidation state that has not previously been observed for crystalline MOF metal nodes. These Rh2+ sites are active for the catalytic hydrogenation of propylene to propane at room temperature, and the MOF structure stabilizes the Rh2+ oxidation state under reaction conditions. Density functional theory calculations suggest a mechanism in which hydrogen dissociation and propylene adsorption occur at the Rh2+ sites. The ability to tailor the geometry and ensemble size of the metal nodes in MOFs allows for unprecedented control of the active sites and could lead to significant advances in rational catalyst design.

REDISPERSION OF COBALT METAL PARTICLES IN Co/TiO2 CATALYST AND ITS EFFECT ON PROPENE HYDROGENATION

Takasaki, Seiji,Takahashi, Kaoru,Suzuki, Hideo,Sato, Yuzuru,Ueno, Akifumi,Kotera, Toyohashi

, p. 265 - 268 (1983)

The rate of propene hydrogenation on Co/TiO2 catalyst, prepared by an alkoxide technique, was significantly enhanced when the catalyst was reduced by hydrogen at 700 deg C.However, over the catalyst prepared by an usual impregnation method, the enhancement of the rate was not observed at any reduction temperatures.The effects of reduction temperatures on the rate of propene hydrogenation were elucidated by redispersion of metallic cobalt particles.

Kinetic Determination of the Gas-Phase Decarbonylation of Butyraldehyde in the Presence of HCl Catalyst

Julio, Libia L.,Cartaya, Loriett,Maldonado, Alexis,Monascal, Yeljair,Mora, José R.,Cordova, Tania,Chuchani, Gabriel

, p. 333 - 338 (2017)

The gas-phase kinetics and mechanism of the homogeneous elimination of CO from butyraldehyde in the presence of HCl has been experimentally studied. The reaction is homogeneous and follows the second-order kinetics with the following rate expression: log k1 (s?1 L mol?1) = (13.27 ± 0.36) – (173.2 ± 4.4) kJ mol?1(2.303RT)?1. Experimental data suggested a concerted four-membered cyclic transition state type of mechanism. The first and rate-determining step occurs through a four-membered cyclic transition state to produce propane and formyl chloride. The formyl chloride intermediate rapidly decomposes to CO and HCl gases.

A stable 16-electron iridium(iii) hydride complex grafted on SBA-15: A single-site catalyst for alkene hydrogenation

Rimoldi, Martino,Fodor, Daniel,Van Bokhoven, Jeroen A.,Mezzetti, Antonio

, p. 11314 - 11316 (2013)

The dihydride pincer complex [IrH2(POCOP)] reacts with surface silanols of mesoporous silica (SBA-15) to give the coordinatively unsaturated, yet stable hydridesiloxo Ir(iii) species [IrH(O-SBA-15)(POCOP)]. The silica-grafted complex catalyses the hydrogenation of ethene and propene at low temperature and pressure without prior activation.

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