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21133-22-2

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21133-22-2 Usage

Check Digit Verification of cas no

The CAS Registry Mumber 21133-22-2 includes 8 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 5 digits, 2,1,1,3 and 3 respectively; the second part has 2 digits, 2 and 2 respectively.
Calculate Digit Verification of CAS Registry Number 21133-22:
(7*2)+(6*1)+(5*1)+(4*3)+(3*3)+(2*2)+(1*2)=52
52 % 10 = 2
So 21133-22-2 is a valid CAS Registry Number.

21133-22-2SDS

SAFETY DATA SHEETS

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

Version: 1.0

Creation Date: Aug 14, 2017

Revision Date: Aug 14, 2017

1.Identification

1.1 GHS Product identifier

Product name 1,5-bis(oxolan-2-yl)pentan-3-one

1.2 Other means of identification

Product number -
Other names 1,5-ditetrahydrofurylpentan-3-one

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only.
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:21133-22-2 SDS

21133-22-2Downstream Products

21133-22-2Relevant articles and documents

Hydrodeoxygenation of furfural-acetone condensation adducts to tridecane over platinum catalysts

Faba, Laura,Díaz, Eva,Vega, Aurelio,Ordó?ez, Salvador

, p. 132 - 139 (2016)

The total hydrodeoxygenation of furfural-acetone condensation adduct (F2A) for obtaining tridecane is studied in this work. Three different Pt catalysts (using alumina, activated carbon, and graphite-MgZr oxide composite as supports) were tested using acetone as solvent (4.5 mmol/L of adduct) in a stirred batch reactor at 493 K and 5.5 MPa. Best results were obtained with Pt/Al2O3, yielding 21.5% of n-tridecane after 24 h reaction time, with carbon balances close to 96%. The performance of the carbon supported catalysts was poorer (both in terms of conversion, tridecane selectivity and carbon mass balance closure) mainly because of the strong adsorption of reactants and reaction intermediates, whereas the MgZr-HSAG also present activity for the undesired cleavage of C-C bonds of the condensation adducts. A kinetic model, considering serial-parallel reaction steps and first order dependence on the organic reactant has been successfully applied for modelling the results obtained with the three catalysts. The dependence of the kinetic constants on the catalyst properties suggest that metal dispersion and the concentration of weak acid sites are the main parameters affecting catalyst performance.

INFLUENCE OF HYDROGEN PRESSURE ON THE RATE AND MECHANISM OF HYDROGENATION OF DIFURFURYLIDENEACETONE IN PRESENCE OF SKELETAL NICKEL-TITANIUM-ALUMINUM CATALYST

Mat'yakubov, R.,Abduganiev, E. G.,Kozhevnikov, V. S.

, p. 1976 - 1978 (2007/10/02)

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