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acetaldehydeanddilactide. In fact,LACcontinues to receive increasedattention for itspoten-
tial use as amonomer in theproductionofbiodegradablepoly lactic acid. It canbeproduced
byeitherbiotechnological fermentationorchemical synthesis,but the formerroute is receiving
considerable interest due to environmental concerns and the limitednature of petrochemical
feedstocks.However, fermentation is inherentlyaslowprocess.Analternativeroute toLACis
by processing a ‘renewable’ resource such as glycerol bymeans of heterogeneous catalysis.
Haruta [2]has reported thatgoldwithparticlediametersbelow10nmare surprisinglyactive
formanyreactions, suchasCOoxidationandpropyleneepoxidation.
Manyaspects of glycerol oxidationbyAuhavebeen studied.Ketchie et al. [3] have lookedat
the effect ofAuparticle size, particularlyonsupports suchas carbon [4] and titania [5],while
Wangetal. [6]haveexamined theeffectofparticle shape,andVillaetal. [7]have investigated
the role of stabilizers in gold sols as catalysts in the liquid-phase oxidation of glycerol. In
addition, Demirel et al. [8] have probed the promotional effect of Pt onAu/C catalysts, and
Royker et al. [9] have investigated the promotional effect of Pt onAu/Al2O3 catalysts,while
other authorshave studied the effect of base in the reaction. For example,Chornaja et al. [10]
examined theoxidationof glycerol toglyceric acidusingPdcatalysts thatworked inalkaline
media, andKetchie et al. [5] reported the promotional effect of hydroxyl ions overAu cata-
lysts,whileCarretin et al. [11] haveanalysed the effect of base as a reaction initiator, proving
that for Au/C catalysts, the presence of OH wasmandatory for any meaningful glycerol
oxidation to occur.However, therewas seemingly very limited studyon the effect of surface
acidity for this reactionusingaluminasupports, forwhich thiswork isdedicated.
2.Experimentalprocedures
2.1.Chemical reagentsandmaterials
Commercialγ-Al2O3support(denotedasDegussa2010,BETspecificsurfaceareaof260m
2g 1),
ammonium molybdate (NH4)6 Mo7O24 4H2O from Associated Chemical Enterprises (ACE),
chloroauricacidHAuCl4 3H2OfromRandRefinery (SouthAfrica),NaOH(98%)andnitric acid
(65%)fromACE,andglycerol (99.5%)fromRochelleChemicalswereused.
2.2.PreparationofMoO3/γ-Al2O3support
Amassof4.6gofγ-Al2O3supportwithameasuredBETspecific surfaceareaof245m
2g 1was
weighedandplacedinabeaker.About100mlsolutionof0.1Mammoniummolybdatesaltwas
measured, enough to formMoO3monolayer coverage at surface concentration of 5 atoms of
metalnm 2 or0.2nm2atom 1 according toStobbe-Kreemerset al. [12]andRaubenheimerand
Cronje [13]. ThepHof the solutionwas thenadjusted to avaluebelow1byadditionofdilute
(0.25M)HNO3acid,with agitation to ensure equaldistributionof the acid to a stablepH.The
supportwas then added to the ammoniummolybdate solution and left to stand for 8 h, after
which, itwas filteredand left to ovendry inair at 120 Cfor 16h. Thedried catalystprecursor
was thencalcined inairat a flowrateof 300SCCMat500 Cfor4h todecomposeanyresidual
ammoniumandnitrate ions fromthesupport, effectively reducing themolybdate ion toMoO3,
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Advanced Chemical Kinetics
- Title
- Advanced Chemical Kinetics
- Author
- Muhammad Akhyar Farrukh
- Editor
- InTech
- Location
- Rijeka
- Date
- 2018
- Language
- English
- License
- CC BY 4.0
- ISBN
- 978-953-51-3816-7
- Size
- 18.0 x 26.0 cm
- Pages
- 226
- Keywords
- Engineering and Technology, Chemistry, Physical Chemistry, Chemical Kinetics
- Categories
- Naturwissenschaften Chemie