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  • 1208169-32-7 Structure
  • Basic information

    1. Product Name: C10H14O
    2. Synonyms: C10H14O
    3. CAS NO:1208169-32-7
    4. Molecular Formula:
    5. Molecular Weight: 150.221
    6. EINECS: N/A
    7. Product Categories: N/A
    8. Mol File: 1208169-32-7.mol
  • Chemical Properties

    1. Melting Point: N/A
    2. Boiling Point: N/A
    3. Flash Point: N/A
    4. Appearance: N/A
    5. Density: N/A
    6. Refractive Index: N/A
    7. Storage Temp.: N/A
    8. Solubility: N/A
    9. CAS DataBase Reference: C10H14O(CAS DataBase Reference)
    10. NIST Chemistry Reference: C10H14O(1208169-32-7)
    11. EPA Substance Registry System: C10H14O(1208169-32-7)
  • 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: 1208169-32-7(Hazardous Substances Data)

1208169-32-7 Usage

Check Digit Verification of cas no

The CAS Registry Mumber 1208169-32-7 includes 10 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 7 digits, 1,2,0,8,1,6 and 9 respectively; the second part has 2 digits, 3 and 2 respectively.
Calculate Digit Verification of CAS Registry Number 1208169-32:
(9*1)+(8*2)+(7*0)+(6*8)+(5*1)+(4*6)+(3*9)+(2*3)+(1*2)=137
137 % 10 = 7
So 1208169-32-7 is a valid CAS Registry Number.

1208169-32-7Upstream product

1208169-32-7Downstream Products

1208169-32-7Relevant articles and documents

Hydrogenation of phenol in supercritical carbon dioxide catalyzed by palladium supported on Al-MCM-41: A facile route for one-pot cyclohexanone formation

Chatterjee,Kawanami,Sato,Chatterjee,Yokoyama,Suzuki

, p. 1912 - 1924 (2009)

The hydrogenation of phenol has been carried out in supercritical carbon dioxide (scCO2) under very mild reaction conditions at the temperature of 50°C over palladium supported Al-MCM-41 (metal loading ~1%). This palladium catalyst is shown to be highly active and promotes the selective formation of cyclohexanone (~98%), an industrially important compound, in a "one-pot~ way. The effects of different variables like carbon dioxide and hydrogen pressure, reaction time and also silica/alumina ratio of the MCM-41 support along with palladium dispersion are presented and discussed. The pressure effect of carbon dioxide is significantly prominent in terms of conversion and cyclohexanone selectivity. Moreover, the silica/alumina ratio was also found to be an important parameter to enhance the effectiveness of the catalyst as it exhibits a remarkable increase in phenol conversion from 20.6% to 98.4% as the support changes from only silica MCM-41 to Al-MCM-41. A plausible mechanism for the hydrogenation of phenol to cyclohexanone over the palladium catalyst has been proposed. The proposition is vali-dated by transition state calculations using density functional theory (DFT), which reveal that cyclohexanone is a favorable product and stabilized by -1 over cyclohexanol in ScCO2 medium. Under similar reaction conditions, phenol hydrogenation was also carried out with rhodium, supported on Al-MCM-41. In contrast to the palladium catalyst, a mixture of cyclohexanone (57.8%) and cyclohexanol (42.2%) was formed. Detailed characterization by X-ray diffraction and transmission electron microscopy confirmed the presence of metal nanoparticles (palladium and rhodium) between 10-20 nm. Both the catalysts exhibit strikingly different product distributions in solventless conditions compared to scCO2. This method can also be successfully applied to the other hydroxylated aromatic compounds.

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