Ms. Luo et Cw. Curtis, EFFECT OF REACTION PARAMETERS AND CATALYST TYPE ON WASTE PLASTICS LIQUEFACTION AND COPROCESSING WITH COAL, Fuel processing technology, 49(1-3), 1996, pp. 177-196
The effect of reaction conditions and catalyst type on the liquefactio
n behavior of model waste plastics and on the coprocessing of model wa
ste plastics with coal was evaluated. Individual model plastics and mi
xtures of these plastics were catalytically reacted at temperatures of
400 to 440 degrees C with an initial H-2 pressure of 5.6 MPa using fl
uid catalytic cracking catalysts and a zeolite HZSM-5. Higher conversi
ons to tetrahydrofuran-soluble material were achieved in the reactions
of individual model plastics than in the reaction with various mixtur
es of model plastics, while higher hexane soluble yields and lower gas
yields were obtained with the mixtures. A base plastics mixture compo
sed of 50% high density polyethylene (HDPE), 30% polyethylene terephth
alate (PET), and 20% polystyrene (PS) was used to evaluate the effect
of reaction time and initial H-2 pressure on the conversions and produ
ct distributions achieved. Reaction times of 120 min produced high and
similar conversions and product distributions from HZSM-5 and two flu
id catalytic cracking catalysts; however, the differences in the three
catalysts' activities were much larger for converting the plastics at
shorter reaction times of 30 and 60 min. The highest conversion of th
e base plastics mixture occurred when the initial H-2 pressure was low
. Addition of aromatic, hydroaromatic, cycloalkane, and straight chain
aliphatic solvents to the base plastics mixture influenced the conver
sion and product distribution obtained. For all three catalysts, the s
traight chain aliphatic solvents were the most effective for solvating
the cracked polymer products and promoting higher conversions. Coproc
essing reactions of the base plastics mixture with coal yielded the hi
ghest conversion when they were reacted catalytically without a solven
t. Introduction of a solvent required higher severity conditions to ac
hieve equivalent conversions as reactions without solvent.