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Would
you like to know:
To
answer the above questions, Linnhoff March
offers fouling monitoring and cleaning cycle
optimisation for refineries.
Fouling
monitoring service
Heat
exchanger fouling profile
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Fouling
petroleum deposits in the preheat train
gradually reduce heat transfer coefficients
and thus your heat recovery. This means
that the furnace inlet temperatures will
drop over time causing energy costs to increase.
Failure to correct this in time may cause
a bottleneck in the furnace and could lead
to even more costly losses in throughput.
Fouling factors and trends, once determined
accurately, can help to avoid these costs.
Heat
transfer coefficients calculated from one
data set can be misleading, because losses
in heat transfer are usually due to a combination
of factors (e.g. heavier crude). To filter
out these interfering effects, you need
rigorous calculations, taking into account
varying feed and product compositions, etc.
Long-term trending also ensures that errors
are minimised.
Linnhoff
Marchs fouling monitoring service
involves rigorous calculation of fouling
factors, using plant data obtained from
a site data historian. This is done in two
steps:
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Data
reconciliation to identify gross errors
in measured flowrates and temperatures |
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Use
of reconciled properties to determine
fouling factors |
Results
are presented in spreadsheet format.
Deliverables
Deliverables from this service are:
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Reconciled
measurements |
These
are useful for accounting purposes and for
other process engineering studies such as
Pinch Analysis.
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Fouling
trend |
Similar
to the one shown above, which can be used
to assess the impact of fouling inhibitors
and operational changes (crude mixes, varying
flowrates, etc) on fouling rates.
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The
Cost of Fouling |
The
cumulative loss in heat recovery and process
throughput will be quantified.
Cleaning
cycle optimisation
The cumulative costs of fouling in terms
of energy and throughput may justify additional
cleaning of strategic exchangers or overall
shorter cleaning cycles. The optimum cleaning
cycle for individual exchangers or for the
entire network can be determined by using
established fouling trends and trading off
the cost of fouling against the cost of
cleaning.

Deliverables are:
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Cleaning
strategy to overcome bottlenecks in
furnace, condensers and pumparounds
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Cleaning
strategy to maximise heat recovery and
minimise fuel requirement |
Why
use Linnhoff March?
Trend
calculations involve the handling of large
amounts of data in a number of simulation
programs. Setting up and carrying out these
calculations is very time-consuming and
leaves considerable room for human-error.
Moreover, commercial programs for network
simulation are unable to incorporate certain
process features, such as pump-around flowrate
limits, to accurately assess the cost of
fouling.
It
takes experienced engineers to incorporate
the specific features of your crude unit
into the analysis. Even for a standard unit,
setting up the necessary data transfers
and calculations requires significant effort.
Linnhoff March has experienced process and
development engineers who are familiar with
all these issues.
Linnhoff
March uses SimScis DATACON for data
reconciliation and HEXTRAN for network rating
and calculation of fouling factors. These
software packages are known for their reliable
physical properties databank for petroleum
refining processes and have been used successfully
for the studies carried out by Linnhoff
March. However, our approach does not depend
on the simulation packages and also works
with other software that will perform these
tasks.
Above
all, Linnhoff March's knowledge of the interactions
in refinery heat exchanger systems is second
to none.
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