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2 www.ipwonline.de6-7/2014
FOCUS ON | PROCESS & QUALITY CONTROL	
in the manner similar to, e.g. trim optimisation solutions
for paper machines, where there are several vendors.
Even in a modern integrated mill that employs sophis-
ticated automation systems, the production schedule is
typically crafted in a manual or semi-manual fashion,
unsupported by a global constraint model and without
the assessment of a specialised software tool with opti-
misation capability.
Production schedulers typically make decisions on the
basis of their experience, calculating set points and stor-
age tank levels heuristically. It is common to find opera-
tors belonging to different shifts to have quite different
views as to what these settings (for the same schedule)
might be. But manual scheduling traditionally lacks vis-
ibility, is time consuming and relies too much on the
planner’s uncertain expertise. ’What-if’ analysis is pre-
cluded as the act of creating a single schedule consumes
all available time. Thus any response to a new situation
becomes a hit-and-miss affair.
Given this situation, there has been academic inter-
est in pulp mill scheduling optimisation since the 80s
(Leiviskä, 1984; Figueira, Santos, & Almada-Lobo, 2013;
Santos & Almada-Lobo, 2012). Studies that analyse how
these algorithms perform in comparison to traditional
scheduling suggest remarkable potential improvements,
e. g. (Lasslett, 2004) found potential production
It combines a state-of-the-art graphical user
interface, with what-if capability & industrial-strength
optimisation into an innovative and unique software
platform.
Effective planning and scheduling is a key factor in the
success of any such operation and one of the few inter-
nally-controllable levers for influencing profitability.
The planning and scheduling functions can be divided,
depending on the time horizon, into four levels:
1. Strategic planning where the time horizon is from
months to several years.
2. Production planning where the time horizon is from
several days to a few months.
3. Production scheduling and control with the time hori-
zon from minutes to a few days.
4. Process control from seconds to minutes sometimes
perhaps hours. This article focuses on level 3.
Somewhat surprisingly, to the best of our knowledge,
there is no commercially-available standard software
using optimisation to address the quite specific needs
for pulp mills. There have been various ad hoc local solu-
tions, but these have not become configurable products,
Greycon
A new tool for optimisation-based
scheduling of pulp mills
By Constantine Goulimis, CEO, Leandro Gomez, Senior Developer  Jari Kaukiainen, Senior Consultant
Modern integrated pulp mills sometimes fail to
reach full economic potential, by relying on manual
approaches for scheduling. Greycon’s recently-
introduced PulpPlan is a new, optimisation based,
scheduling system for pulp mills.
Pulp production in an integrated pulp and paper mill
Time hierarchy in planning  scheduling
36-7/2014
FOCUS ON | PROCESS  QUALITY CONTROL

to build stock and also to make the best use of the
available capacity in the storage tanks in these critical
scenarios.
One particular aspect needs further attention: any
complex but sequential multi-stage operation needs to
mitigate against failures of any one stage. A stochastic
failure model can provide the basis for determining opti-
mal levels for intermediate storage tanks. If the system
finds the processes downstream of any storage tank are
very unreliable compared to those that are upstream,
it will set a low target stock level for that storage tank.
Integration  key functionality
Integration is a key requirement for successful imple-
mentation. PulpPlan accepts information from the dif-
ferent production areas across the mill. The distributed
control system (DCS) provides, either directly or via a
data historian, current stock levels and process rates
of all the production areas. This includes the pulping,
recovery and recaustization lines. Similarly, an interface
with the block scheduling system allows importing the
schedule of the paper machines.
The operator uses a graphical user interface to under-
stand, experiment with and decide on the schedule.
Another area targeted by the optimisation is the brown-
stock washing efficiency. The optimisation engine calcu-
lates the optimal dilution factor so as to minimise cost.
This calculation considers the costs of bleach chemical
consumption, soda loss and evaporator steam versus
dilution factor. However, the optimal dilution factor
is affected by evaporator performance; the latter can
reduce the throughput of the whole mill. Thus efficiency
depends on the dynamic load of the recovery system as
well as the paper machine block schedule. The resulting
increases of 5 % simply by better coordinating pulp and
recovery lines.
The actual benefits obtained will of course vary from
mill to mill. Mills where production constraints are
dynamic and pulp production is directly linked with
the block schedule for the paper machines are the ones
which have the most potential for improvement. But
other pulp producers can also benefit. Their expected
gains will depend mainly on mill complexity and market
dynamics.
In coming up with PulpPlan we decided to exploit
today’s computational power, in order to deliver the
required operational efficiency improvements using a
combination of: a familiar user interface that includes
a graphically-configured mathematical model of the
whole pulp mill, non-linear mathematical optimisation
technology that can determine realistic optimised sched-
ules in just in few seconds and what-if capability to allow
uninhibited scenario exploration (as well as forming an
educational platform).
In general, the goal of pulp production scheduling is to
ensure that production targets are met while produc-
tion costs are minimised. PulpPlan takes that concept
a step further, as it is designed to produce perfectly
coordinated production plans for the whole mill so
that: Production is maximised with respect to demand;
Production costs are minimised; Process rate changes
are minimised: Target stock levels are reached; Even
distribution of available stock in times of shortage and
Constraints are respected.
Optimising the performance of any system under a
dynamic environment can be challenging and time con-
suming. Production scheduling can be used to identify
quickly current and future constraints and take the
proper actions to maximise production under the cur-
rent scenario. For instance, in the case of high demand
periods, scheduling can be used to detect the need
Inputs for the pulp scheduler
Pulp line status screen
4 www.ipwonline.de6-7/2014
FOCUS ON | PROCESS  QUALITY CONTROL	
Cost analysis
plan maximises efficiency for the whole mill, not just the
sub-processes.
In mills where steam generation takes place in two or
more boilers and/or using different fuels, cost optimi-
sation can be a challenging task without the proper
software tool. Optimisation algorithms use production
plans to determine the optimal fuel load for each boiler,
thus helping to save costs and meet environmental con-
straints (such as limit in the total reduced sulphides). If
optimising carbon dioxide emissions takes precedence
over reducing expenses, then the optimisation engine
can be easily reconfigured to reduce CO2 instead of
costs.
References
Figueira, G., Santos, M. O.,  Almada-Lobo, B. (2013).
A hybrid VNS approach for the short-term production plan-
ning and scheduling: A case study in the pulp and paper
industry. Computers and Operations Research, 1804-1818.
Lasslett, N. (2004).
Smart Scheduling of Pulp Mills  Chemical Recoveries. 58th
Appita Annual Conference 2004 Proceedings.
Leiviskä, K. (1984).
Short term production scheduling of the pulp mill – A decen-
tralized optimization approach. In Lecture Notes in Control
and Information Sciences (Vol. 59, pp. 780-789). Springer
Berlin Heidelberg.
Santos, M. O.,  Almada-Lobo, B. (2012).
Integrated pulp and paper mill planning and scheduling.
Computers  Industrial Engineering, 63, 1-12.
While the economic value of increased output and
reduced production costs is evident, there are other less
obvious benefits that would result from more stable
operation. Fewer and smaller production rate changes
(i.e. stabilizing continuous digesters, washers and bleach
plant operation) will result in less variability in pulp qual-
ity. Operational costs are also expected to be reduced
by better pulp inventory management. For example,
lowering the level of pulp on offline storages will reduce
the amount of double handling and energy required to
press pulp, dump it and reclaim it.
PulpPlan promises a ROI of less than two months based
on: higher production throughput, reduced cost and
fast, accurate response to changing conditions. ■

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Modern pulp mills optimisation software maximises production

  • 1. 2 www.ipwonline.de6-7/2014 FOCUS ON | PROCESS & QUALITY CONTROL in the manner similar to, e.g. trim optimisation solutions for paper machines, where there are several vendors. Even in a modern integrated mill that employs sophis- ticated automation systems, the production schedule is typically crafted in a manual or semi-manual fashion, unsupported by a global constraint model and without the assessment of a specialised software tool with opti- misation capability. Production schedulers typically make decisions on the basis of their experience, calculating set points and stor- age tank levels heuristically. It is common to find opera- tors belonging to different shifts to have quite different views as to what these settings (for the same schedule) might be. But manual scheduling traditionally lacks vis- ibility, is time consuming and relies too much on the planner’s uncertain expertise. ’What-if’ analysis is pre- cluded as the act of creating a single schedule consumes all available time. Thus any response to a new situation becomes a hit-and-miss affair. Given this situation, there has been academic inter- est in pulp mill scheduling optimisation since the 80s (Leiviskä, 1984; Figueira, Santos, & Almada-Lobo, 2013; Santos & Almada-Lobo, 2012). Studies that analyse how these algorithms perform in comparison to traditional scheduling suggest remarkable potential improvements, e. g. (Lasslett, 2004) found potential production It combines a state-of-the-art graphical user interface, with what-if capability & industrial-strength optimisation into an innovative and unique software platform. Effective planning and scheduling is a key factor in the success of any such operation and one of the few inter- nally-controllable levers for influencing profitability. The planning and scheduling functions can be divided, depending on the time horizon, into four levels: 1. Strategic planning where the time horizon is from months to several years. 2. Production planning where the time horizon is from several days to a few months. 3. Production scheduling and control with the time hori- zon from minutes to a few days. 4. Process control from seconds to minutes sometimes perhaps hours. This article focuses on level 3. Somewhat surprisingly, to the best of our knowledge, there is no commercially-available standard software using optimisation to address the quite specific needs for pulp mills. There have been various ad hoc local solu- tions, but these have not become configurable products, Greycon A new tool for optimisation-based scheduling of pulp mills By Constantine Goulimis, CEO, Leandro Gomez, Senior Developer Jari Kaukiainen, Senior Consultant Modern integrated pulp mills sometimes fail to reach full economic potential, by relying on manual approaches for scheduling. Greycon’s recently- introduced PulpPlan is a new, optimisation based, scheduling system for pulp mills. Pulp production in an integrated pulp and paper mill Time hierarchy in planning scheduling
  • 2. 36-7/2014 FOCUS ON | PROCESS QUALITY CONTROL to build stock and also to make the best use of the available capacity in the storage tanks in these critical scenarios. One particular aspect needs further attention: any complex but sequential multi-stage operation needs to mitigate against failures of any one stage. A stochastic failure model can provide the basis for determining opti- mal levels for intermediate storage tanks. If the system finds the processes downstream of any storage tank are very unreliable compared to those that are upstream, it will set a low target stock level for that storage tank. Integration key functionality Integration is a key requirement for successful imple- mentation. PulpPlan accepts information from the dif- ferent production areas across the mill. The distributed control system (DCS) provides, either directly or via a data historian, current stock levels and process rates of all the production areas. This includes the pulping, recovery and recaustization lines. Similarly, an interface with the block scheduling system allows importing the schedule of the paper machines. The operator uses a graphical user interface to under- stand, experiment with and decide on the schedule. Another area targeted by the optimisation is the brown- stock washing efficiency. The optimisation engine calcu- lates the optimal dilution factor so as to minimise cost. This calculation considers the costs of bleach chemical consumption, soda loss and evaporator steam versus dilution factor. However, the optimal dilution factor is affected by evaporator performance; the latter can reduce the throughput of the whole mill. Thus efficiency depends on the dynamic load of the recovery system as well as the paper machine block schedule. The resulting increases of 5 % simply by better coordinating pulp and recovery lines. The actual benefits obtained will of course vary from mill to mill. Mills where production constraints are dynamic and pulp production is directly linked with the block schedule for the paper machines are the ones which have the most potential for improvement. But other pulp producers can also benefit. Their expected gains will depend mainly on mill complexity and market dynamics. In coming up with PulpPlan we decided to exploit today’s computational power, in order to deliver the required operational efficiency improvements using a combination of: a familiar user interface that includes a graphically-configured mathematical model of the whole pulp mill, non-linear mathematical optimisation technology that can determine realistic optimised sched- ules in just in few seconds and what-if capability to allow uninhibited scenario exploration (as well as forming an educational platform). In general, the goal of pulp production scheduling is to ensure that production targets are met while produc- tion costs are minimised. PulpPlan takes that concept a step further, as it is designed to produce perfectly coordinated production plans for the whole mill so that: Production is maximised with respect to demand; Production costs are minimised; Process rate changes are minimised: Target stock levels are reached; Even distribution of available stock in times of shortage and Constraints are respected. Optimising the performance of any system under a dynamic environment can be challenging and time con- suming. Production scheduling can be used to identify quickly current and future constraints and take the proper actions to maximise production under the cur- rent scenario. For instance, in the case of high demand periods, scheduling can be used to detect the need Inputs for the pulp scheduler Pulp line status screen
  • 3. 4 www.ipwonline.de6-7/2014 FOCUS ON | PROCESS QUALITY CONTROL Cost analysis plan maximises efficiency for the whole mill, not just the sub-processes. In mills where steam generation takes place in two or more boilers and/or using different fuels, cost optimi- sation can be a challenging task without the proper software tool. Optimisation algorithms use production plans to determine the optimal fuel load for each boiler, thus helping to save costs and meet environmental con- straints (such as limit in the total reduced sulphides). If optimising carbon dioxide emissions takes precedence over reducing expenses, then the optimisation engine can be easily reconfigured to reduce CO2 instead of costs. References Figueira, G., Santos, M. O., Almada-Lobo, B. (2013). A hybrid VNS approach for the short-term production plan- ning and scheduling: A case study in the pulp and paper industry. Computers and Operations Research, 1804-1818. Lasslett, N. (2004). Smart Scheduling of Pulp Mills Chemical Recoveries. 58th Appita Annual Conference 2004 Proceedings. Leiviskä, K. (1984). Short term production scheduling of the pulp mill – A decen- tralized optimization approach. In Lecture Notes in Control and Information Sciences (Vol. 59, pp. 780-789). Springer Berlin Heidelberg. Santos, M. O., Almada-Lobo, B. (2012). Integrated pulp and paper mill planning and scheduling. Computers Industrial Engineering, 63, 1-12. While the economic value of increased output and reduced production costs is evident, there are other less obvious benefits that would result from more stable operation. Fewer and smaller production rate changes (i.e. stabilizing continuous digesters, washers and bleach plant operation) will result in less variability in pulp qual- ity. Operational costs are also expected to be reduced by better pulp inventory management. For example, lowering the level of pulp on offline storages will reduce the amount of double handling and energy required to press pulp, dump it and reclaim it. PulpPlan promises a ROI of less than two months based on: higher production throughput, reduced cost and fast, accurate response to changing conditions. ■