accepted standards, such as the European best available
technique (BAT). Inefficiencies are identified and
improvement measures are recommended according
to the level of detail and quality of the information
gathered. Some relevant outcomes from VDZ’s energy
reviews are presented below.
Thermal energy consumption
In order to assess the performance level of a cement
plant with respect to its thermal energy consumption, a
comparison with BAT and reviewer performance indicators
is made. The BAT performance level without using AFs,
mentioned in the European BAT reference document
(BREF) for the cement industry, is 2900 – 3300 MJ/t
clinker for a 3000 tpd kiln.
3
This level should be seen as a
performance level that can be achieved under optimum
conditions in a short term performance test. The European
BREF also states that on a yearly level the energy demand
can be 160 – 320 MJ/t clinker higher because of heating up
and shutting down the kiln, unplanned kiln stops, etc. This
results in a BAT range on a yearly level of 3160 – 3320 MJ/t
clinker (using 3000 MJ/t clinker as a basis). Experience
shows that the use of AFs, depending on their physical
and chemical properties, often leads to an increase in the
fuel energy demand of cement kilns. Based on process
modelling, the relation between fuel energy demand
and AF ratio was determined.
2
The AF mix that was taken
as a basis comprises several typical AFs being used in the
cement industry. The modelling – as well as the European
BREF document – considers a precalciner kiln with a
five-stage preheater. Furthermore, data from the CSI’s
Getting the Numbers Right (GNR) database have been
considered. It has to be highlighted that a careful and
methodical assessment is required when comparing real
plant data with BAT, as plant specific conditions must be
taken into account. Figure 1 shows data from kiln lines
that VDZ was asked to review. As production capacity also
influences the specific energy demand, the figure only
depicts kilns of the same size, in this case with production
capacities of about 3000 tpd. Similar schemes are also
available for other kiln capacities (e.g. 1500 and 5000 tpd).
The diagram shows that most of the kiln lines reviewed
had a fuel energy demand higher than the BAT range,
which uncovers potential for optimisation. The following
factors can be related to these potentials:
z
Technological factors (type of equipment and
equipment design).
z
Operational factors (thermal substitution rate, kiln
instability, coating formation, blockages, refractories,
and frequent kiln starts and shutdowns for process
reasons, etc.).
z
Maintenance factors (kiln seal condition,
preheater and calciner condition, kiln stops due to
malfunction of equipment, and lack of calibration of
instrumentation, etc.).
z
Quality factors (fuels, raw materials and raw
mix chemical and physical properties, and LSF
fluctuation).
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