شماره ركورد كنفرانس :
5048
عنوان مقاله :
Maximization Of Propylene In FCC Process By Adding ZSM-5 Additive to FCC Catalyst
Author/Authors :
Farshi ،A department West Side of Azadi sport complex - Tehran، Iran , Bazyari ،A department West Side of Azadi sport complex - Tehran، Iran , Borogerdi ،S.H department West Side of Azadi sport complex - Tehran، Iran , Daneshvar ،A department West Side of Azadi sport complex - Tehran، Iran , Abri ،H.R department West Side of Azadi sport complex - Tehran، Iran
كليدواژه :
FCC , Propylene , Yield , Additive , ZSM-5
عنوان كنفرانس :
ششمين كنگره بين المللي مهندسي شيمي
چكيده لاتين :
FCC units are present in most refineries for production of gasoline, LPG and middle distillates, representing a conversion
capacity above 14 MMBPD. FCC also plays an increasing role in residue conversion with now more than 4 MMBPD of
RFCC capacity in the world and accounts for more and more of the propylene market(with more than 25% of propylene
world production coming from FCC gas plants)[5].The effects of operating parameters such as reaction temperature, and
ZSM-5 as FCC catalyst additive, on the distribution of the product and the yield of propylene were investigated on a bench
scale fluidized bed reactor. It is the aim of this work to perform an overall analysis of the yields and selectivity of
hydrocarbons obtained in the vacuum gas oil conversion over FCC and ZSM-5 catalysts .The effectiveness of ZSM-5
additive adding in FCC process was investigated. The experimented data of off gas analysis showed that, VGO cracking at
high reaction temperatures of 450–550°C increases the yield of propylene. Similar behavior is observed with the addition
of 10–25 wt.% ZSM-5 additive. The combination of the two effects (high temperature and ZSM-5 addition) makes the
FCC unit an excellent source of light olefins for downstream petrochemical units. Higher FCC reactor temperatures (600-
650°C) would not have positive effect for increasing propylene yield.