LEADER 01777nam  2200385z- 450 
001 9910346706103321
005 20210211
010   $a1000007336
035   $a(CKB)4920000000094633
035   $a(oapen)https://directory.doabooks.org/handle/20.500.12854/55713
035   $a(oapen)doab55713
035   $a(EXLCZ)994920000000094633
100   $a20202102d2008      u|         0
101 0 $aeng
135   $aurmn|---annan
181   $ctxt$2rdacontent
182   $cc$2rdamedia
183   $acr$2rdacarrier
200 00$aPartial oxidation of Raffinate II and other mixtures of n-Butane and n-Butenes to maleic anhydride in a fixed-bed reactor
210   $cKIT Scientific Publishing$d2008
215   $a1 online resource (VI, 186 p. p.)
311 08$a3-86644-199-1 
330   $aThe utilisation of the C4 streams of steamcrackers by converting raffinate II to maleic anhydride was studied. The oxidation reactions were investigated in a laboratory-scale fixed-bed reactor to determine reaction kinetics. The effects of pore diffusional resistance were investigated and explained. A two-dimensional pseudo-homogeneous reactor model was used for the simulation of a production-scale fixed-bed reactor. A flow scheme of the reactor section including a recycle was proposed.
606   $aBiotechnology$2bicssc
610   $aMaleic Anhydride
610   $aPartial Oxidation
610   $aRaffinate II
610   $aReaction Kinetics
610   $aReactor Simulation
615  7$aBiotechnology
700   $aBrandstädter$b Willi Michael$4auth$01291433
906   $aBOOK
912   $a9910346706103321
996   $aPartial oxidation of Raffinate II and other mixtures of n-Butane and n-Butenes to maleic anhydride in a fixed-bed reactor$93021838
997   $aUNINA