Previous efforts were made to convert the oil sludge into useful resources such as lower molecule
organic compounds and carbonaceous residues by pyrolysis with the carrier gas of N2. The liquid
products (condensates of gases at 298 K) obtained from the pyrolysis of oil sludge are close to
diesel oil. However, they contain a significant amount of vacuum residues of about 9.57 wt %,
which decrease the qualities of liquid products. In the present study, the oil sludge from the oil
storage tank of a typical petroleum refinery plant located in the northern Taiwan is used as the
raw material for the pyrolysis. The influences of using inexpensive and nonharmful additives on
the possible improvement of the pyrolysis of oil sludge are investigated. The additives employed
include two groups: (1) aluminum compounds (Al, Al2O3, and AlCl3), and (2) iron compounds
(Fe, Fe2O3, FeSO4
·7H2O, FeCl3, and Fe2(SO4)3
·nH2O). For the increases of conversion X, the
additives provide the offers on the order of Fe2(SO4)3
·nH2O > Fe2O3 > AlCl3 > FeSO4
·7H2O >
Al2O3 > FeCl3 > Al > Fe > no additives. It appears that the above additives enhance the reaction
rates r when the temperatures T are in 650−710 K, following the orders AlCl3 > Al > Al2O3 >
no additives, and Fe2O3 ∼ Fe2(SO4)3
·nH2O > FeCl3 ∼ Fe ∼ FeSO4
·7H2O > no additives at 710 K.
The additives achieve the improvement of the quality q of the oil of pyrolysis (as sum of light
and heavy naphtha and light gas oil) on the order of Fe2O3 > Fe2(SO4)3
·nH2O > no additives >
Al > FeSO4
·7H2O > Al2O3 > Fe > FeCl3 > AlCl3. Nevertheless, the additives improve the liquid
yields Y on the order of Al > Fe2(SO4)3
·nH2O > Fe > Fe2O3 > FeCl3 > no additives > AlCl3 >
FeSO4
·7H2O > Al2O3. All this information is useful not only to the improvement of a pyrolysis
system but also to the better utilization of liquid oil products.