Pellet- and reactor-scale models for Fischer–Tropsch
synthesis
(FTS) with a Fe–K/silica catalyst were developed to investigate
the sensitivity of the hydrocarbon products and carbon dioxide selectivity
to process conditions and feed composition at high temperature (350–400
°C), moderate pressure (1–10 bar), and a range of H2/CO ratios (3–1). The major objective of this paper
is to develop, validate, and evaluate a high-temperature FTS model
that is then used to assess the feasibility of process integration
with syngas production. Since there is limited kinetic data available,
in literature at these conditions, bench-scale reactor tests were
conducted to obtain operational data for parameter fitting of kinetic
expressions used in the model. This resulting kinetic model demonstrated
agreement with the experimental data with an R
2 of 0.97 to the testing data set and, thus, was feasible to
apply at pellet and reactor scales. Multiple pellet sizes were modeled
to detail the role of transport limitations as the sphere’s
diameter approached and exceeded 1 mm. Application of the reactor
model indicated that hydrocarbon selectivity depended strongly on
temperature, whereas the ratio of olefin to paraffin products decreased
with increasing temperature, pressure, and H2/CO ratio.
Product selectivity was not sensitive to the conversion of carbon
monoxide. Furthermore, the roles of the pressure and H2/CO ratio were closely coupled. At a H2/CO ratio of 3,
only slight variations in selectivity occurred over a pressure range
of 1–20 bar, whereas at a ratio of 1, selectivity could vary
by as much as 30% over the same pressure range. At pressures below
5 bar and temperatures above 350 °C, minimal selectivity to heavy
hydrocarbons (C12+) is obtained, and selectivity to midrange
products (C5–11) rapidly declined as pressure dropped
below 5 bar, which indicated that an operational pressure of at least
5 bar is needed to achieve reasonable yields in this temperature range.
These results, while tentative, provide guidelines for further experimentation
and evaluation of integrated FTS processes.