Title of article
Degradation of LDPE/VGO mixtures to fuels using a FCC equilibrium catalyst in a sand fluidized bed reactor Original Research Article
Author/Authors
Antonio Marcilla، نويسنده , , Ma del Remedio Hern?ndez، نويسنده , , ?ngela N. Garc?a، نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2008
Pages
11
From page
181
To page
191
Abstract
Plastic degradation for recovery of useful products or raw materials is a very interesting alternative for reducing the plastic accumulation. This paper explores the possibility of using refinery facilities to carry out the plastic cracking as well as to take the most of the products obtained. In the present work, LDPE/VGO blends with different percentages of polymer are degraded in presence of a FCC equilibrium catalyst. The reactor used in this study is a laboratory scale sand fluidized bed reactor at 500 °C, and a 7:1 catalyst:LDPE/VGO blend ratio in order to simulate the operating conditions in a large scale industrial reactor. Polyethylene blends evaluated show relative proportions of LDPE of 0, 6, 25, 75 and 100% (w/w). Gas and liquid compounds were collected and quantified. The results obtained are compared with those generated in a thermal cracking.In all cases, the FCC equilibrium catalyst showed a high selectivity to the production of isobutane and isopentane in the volatile compounds as well as to aromatics in the liquid products.Results shown in this paper evidences the viability of introducing plastics into FCC unit, producing potential valuable products from low value materials.
Keywords
Low-density polyethylene , Fluid catalytic cracking catalyst (FCC) , Equilibrium catalyst , Flash pyrolysis , Low-density polyethylene–vacuum gas oil blend , Vacuum gas oil , Fluidized bed reactor
Journal title
Applied Catalysis A:General
Serial Year
2008
Journal title
Applied Catalysis A:General
Record number
1153673
Link To Document