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Multi-Area Transformation
Pulp & Paper Company, Australasia

Pulp & Paper

Multi-Area Transformation

Multi-Area Transformation
Pulp & Paper Company, Australasia
Multi-Area Transformation

Multi-Area Transformation

Multi-Area Transformation
Executive Summary

€1.46 MEUR without Capital Expenditure

Over a 24-month programme, we embeddedeleven model-predictive-control (MPC) and soft-sensor applications across thedigester, evaporators, recovery boiler and steam network. The phased roll-outhas delivered ≈ EUR 1.46 million every year in steady-state savings andrevenue uplift. Headline wins include + 53 t/day pulp throughput, + 9 344MWh/yr power export, and a 1.2 % boiler-efficiency lift.

Client Background

900 kTon Bleached Pulp Mill

Operating for more than six decades, this coastal Australasian kraft complex converts sustainably managed plantation hardwood into ≈ 900 000 t of bleached pulp per year, supplying packaging customers worldwide. A single recovery boiler supplies all site steam and drives a back-pressure turbine that exports green electricity to the grid.

Problem

Hidden Bottlenecks & Fragmented Processes

When the client contacted us, they struggled with numerous challenges

  • Escalating electricity tariffs – grid prices rose ≈ 80 % in four years.
  • Fibre-cost pressure – hardwood indices remain ≈ 27 % above 2019 levels.
  • Sustainability mandate – corporate roadmap targets a 10–25 % cut in steam- and water-intensity while lifting output to meet demand.

Isolated fixes merely shifted constraints: speeding up the digester exposed evaporator limits; boiler water-wash downtime erased cycle-time gains. Variable controls, manual soot-blowing and liquor-density swings kept the mill from realising sustained benefit.

Some of their key pain points were

  • Digester cook-time buffers masked true capacity.
  • Liquor-solids excursions triggered unplanned evaporator drains.
  • Fixed-interval soot-blowing wasted steam and forced wash shuts.
  • Steam-header pressure spikes throttled turbine generation.

Solution

Anssum's Three Step Solution Framework

Facing multiple challenges at the client’s mill, we adopted a targeted approach using Anssum’s three-step solution framework:

  • Data-Driven Discovery: Uncovering insights through precise analysis.
  • Collaborative Design: Co-creating tailored solutions with the client.
  • Straightforward Integration: Implementing seamlessly for lasting impact.

John Doe

Implementation Process

Step What We Did Operator Role
1 Data-Driven Discovery 14-day historian scrape fed into mass-balance & energy models; constraints ranked by financial impact. Flagged "pain-shift" events when one area sped up.
2 Collaborative Design Built 11 MPC & soft-sensor blocks for cycle-time, liquor density, soot-blowing and steam-header control. Piloted each block in shadow mode; fine-tuned constraints.
3 Straightforward Integration Algorithms embedded in the existing DCS – no hardware cap-ex. Dashboards flag new constraints in real time. Approved HMIs; two half-day training sessions.
Results

1.45 MEUR Steady State Gain

Initiative Challenge Addressed Outcomes
Cycle-Time Compression Long H-factor buffer +53 t/day pulp
Smart Soot-Blowing Fixed 30-min cycles 0 water-wash shuts in 12 mo
Evaporator Density Control Liquor-solids excursions Steam economy +2%
Steam-Header MPC Header pressure spikes +9,344 MWh/yr export

Financial Summary – ≈ EUR 1.4million/year steady-state; 6 Month ROI.

Takeaways

Key Takeaways

Iterative Bottleneck Removal – each MPC block frees the next constraint, compounding gains.

Operator-Friendly Integration – running inside the existing DCS secures trust and rapid uptake.

Sustainability Meets Profitability – steam, fibre and power savings align with CO₂-intensity goals.

Holistic View = Greater ROI – treating the mill as a single system outperforms piecemeal fixes.

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