Abstract: In recent years, the failure accidents in petrochemical industry have been frequent, and have posed great security problems in personnel and property. The improvement of petrochemical safety is highly requested in order to prevent re-occurrence of severe accident. This study focuses on surveying the failure cases occurred in petrochemical field, which were extracted from journals of engineering failure, including engineering failure analysis and case studies in engineering failure analysis. The relation of failure mode, failure mechanism, type of components, and type of materials was analyzed in this study. And the analytical results showed that failures occurred more frequently in vessels and piping among the petrochemical equipment. Moreover, equipment made of carbon steel and stainless steel accounts for the majority of failures compared to other materials. This may be related to the application of the equipment and the performance of the material. In addition, corrosion failures were the largest in number of occurrence in the failure of petrochemical equipment, in which stress corrosion cracking accounts for a large proportion. This may have a lot to do with the service environment of the petrochemical equipment. Therefore, it can be concluded that the corrosion prevention of petrochemical equipment is particularly important.
Abstract: Waste polyethylene (PE) is classified as waste low
density polyethylene (LDPE) and waste high density polyethylene
(HDPE) according to their densities. Pyrolysis of plastic waste may
have an important role in dealing with the enormous amounts of
plastic waste produced all over the world, by decreasing their
negative impact on the environment. This waste may be converted
into economically valuable hydrocarbons, which can be used both as
fuels and as feed stock in the petrochemical industry. End product
yields and properties depend on the plastic waste composition.
Pyrolytic biochar is one of the most important products of waste
plastics pyrolysis. In this study, HDPE and LDPE plastic wastes were
co-pyrolyzed together with waste olive pomace. Pyrolysis runs were
performed at temperature 700°C with heating rates of 5°C/min.
Higher pyrolysis oil and gas yields were observed by the using waste
olive pomace. The biochar yields of HDPE- olive pomace and LDPEolive
pomace were 6.37% and 7.26% respectively for 50% olive
pomace doses. The calorific value of HDPE-olive pomace and
LDPE-olive pomace of pyrolysis oil were 8350 and 8495 kCal.