Vol.:(0123456789) 1 3
J Polym Environ
DOI 10.1007/s10924-017-1053-y
ORIGINAL PAPER
Effect of Microstructure of High Density Polyethylene
on Catalytic Degradation: A Comparison Between Nano Clay
and FCC
Abbas Kebritchi
1,2
· Mehdi Nekoomansh
1
· Fereidoon Mohammadi
1
·
Hossein Ali Khonakdar
1,2
© Springer Science+Business Media, LLC 2017
(LLDPE) from its first commercialization in the late 1970s
has seen the fastest growth rate in usage of the three major
polyethylene families—low density polyethylene (LDPE),
LLDPE, and high density polyethylene (HDPE)—and now
comprises approximately 25% of the annual production of
polyethylene around the world approaching 13 million met-
ric tons [2]. However polyolefins (polyethylene and poly-
propylene) amount almost to the half of plastic wastes [3].
Owing to the limited capacity of landfill sites, increasing
disposal costs, the generation of greenhouse gases (such as
methane) and poor biodegradability of plastic wastes the
common practice of discarding plastic wastes to landfill is
becoming undesirable [1, 4–6].
From another point of view, plastic waste can be
regarded as a potentially cheap source of chemicals and
energy [7–9]. Feedstock recycling as an attractive tech-
nique has attracted much attention aiming to convert waste
polymer materials into original monomers or into other val-
uable chemicals [10–12]. It is certainly possible to develop
commercial processes based on equilibrium fluid catalytic
cracking (FCC). Therefore, a more interesting approach is
that of adding polymer waste into the FCC process, under
suitable process conditions with the use of zero value of
equilibrium FCC catalysts, a large number of waste plastics
can be economically converted into valuable hydrocarbons.
However, much less is known about the performance of
FCC commercial catalysts on the degradation of polymer
waste [13].
Fluid catalytic cracking (FCC) catalysts are made using
zeolite particles dispersed on an amorphous silica–alumina
matrix. Since 1960, the most used zeolite in this kind of
catalysts is the Y zeolite [14]. The FCC catalysts have good
product selectivity [15] and usually have faujasite struc-
ture with a ratio of Si/Al greater than 1.5. This catalyst is
formed by the arrangement of truncated octahedra forming
Abstract The effect of microstructure of high density
polyethylene (HDPE) on catalytic degradation over fluid
catalytic cracking (FCC) catalyst and Nano clay is investi-
gated. An ethylene/1-hexene copolymer (HDPE) was frac-
tionated based on 1-hexene content to different fractions
using preparative temperature rising elution fractionation
(P-TREF) method. The short chain branch (SCB) content
of each fraction calculated based on
1
H NMR results. The
homogenous SCB content fractions were subsequently ana-
lyzed using TGA and thermal degradation behavior of sam-
ples were compared with catalytic degradation. The results
showed that FCC, in contrast to nano clay, is more sensitive
to microstructure of HDPE during catalytic degradation.
Therefore, linear chains can start degradation sooner on
FCC than the branched chains. In comparison of nano clay
and FCC it was found that the nano clay, reduces tempera-
ture at maximum degradation rate (T
max
), but FCC reduces
the T
5%
and T
max
significantly.
Keywords Microstructure · High density polyethylene ·
Catalytic degradation · FCC and nano clay
Introduction
Our modern society is unimaginable without plastics such
as polyethylenes [1]. Linear low density polyethylene
* Abbas Kebritchi
a.kebritchi@ippi.ac.ir
1
Iran Polymer and Petrochemical Institute, 14965-115 Tehran,
Iran
2
Leibniz-Institut für Polymerforschung Dresden e.V.,
01069 Dresden, Germany