
AZURA® SMB system instructions V6775
10 Simulated Moving Bed principle
In Fig.10 the concentrations are normalized on the feed concentration of
each component. These normalized concentrations are plotted versus the
time coordinate. There are typical zigzag profiles, where a triangle sym-
bolizes one switching interval or tact. After 12 of these intervals (i.e. 3 full
cycles for a four column SMB process) the cyclic steady state is reached
(two proceeding triangles are almost identical). By integrating the profiles
over the time range, the averaged concentration can be calculated, i.e. the
concentration measured in a vessel.
Since only four columns (minimal number) are supposed in simulating-
Fig.10 the separation performance is low, i.e. there are impurities of the
other component in each outlet. Increasing the number or the length of the
columns would increase the separation performance.
2.5 Eciency and economic aspects
Chromatographic separation processes belong to the expensive ones,
compared with other thermal separation processes (distillation, crys-
tallization, etc.). This is caused by high prices for the adsorbents (e.g.
spherical silica gel in a high quality, chemically modified) and by the pure
solvents needed.
Nevertheless, chromatographic processes are very eective. They are
suitable for dicult separation problems, where the mixture compounds
have very similar physico-chemical properties as well as for the separa-
tion of very expensive products. This is fulfilled for many products of the
pharmaceutical and fine chemical industry or the food and drug industry.
In these industries some compounds are produced, which can only be
separated by chromatography.
In the previous chapters, three chromatographic modes were described
(elution, TMB, SMB). Out of these modes preparative elution chromato-
graphy is theoretically as well as practically the best known one. It has
been applied for a long time and creates the standard, at that new met-
hods are measured.
The modes are suitable for preparative scale processes. These scales can
be very dierent ones: While in petrol-chemistry 100,000 metric tons per
annum are produced, in the pharmaceutical industry only a few kilograms
are produced. From an industrial point of view only elution chromatogra-
phy and the SMB process are attractive out of the three modes, due to
the diculties connected with the solid movement in TMB.
To compare the two important modes (elution, SMB) in a fair way, the
plant scale has to be considered. After optimization of the two modes
dierent optimal points in the multidimensional space of process relevant
parameters are reached.
Such parameters are in the elution mode the volumetric flow rate of
the eluent, the injected amount of the mixture per pulse, the time gap
between two pulses, the produced amounts of purified compound, the
column geometry, the properties of the column packing, the required
purity, the temperature, etc. In SMB the volumetric flow rates (solid and
liquid) in each zone, the number of columns and the column geometry,
the produced amounts of purified compounds, the feed and withdrawal
concentrations, the properties of the column packing, the required purity,
the temperature etc. are relevant. Both modes are suitable for various
separation tasks. The specific problem, hence, has to been known for a
fair comparison.