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Asset Optimization - Performance Monitoring & Optimization Division













 
 
Shell Nederland saves over $1.7M from the application of AMS Suite: Real-Time Optimizer
 
Return to Customer Proven
 
 

Customer Proven Results  
 
Independently assessed savings of $1.7M* per year
Optimal furnace conditions and back-end setpoints
Optimal feedstock selection and allocation
Improved forecasting
Project payback of less than 6 months

Challenge


The Moerdijk olefins plant is primarily concerned with the production of ethylene and propylene by cracking a range of input feeds. The process is complicated by the ability to bring in feedstocks directly to the back-end of the plant and by the options which are available to process the by-products of the cracking process. Shell Nederland Chemie’s objectives were to increase the cost effectiveness of the plant per tonne/throughput by determining within the context of the plant as a whole:

The optimal furnace operating feed rates and conditions
The optimal rates for the back-end feedstocks
The optimal routing of process fluids through the back-end of the plant
The optimal feedstock - based on availability

Solution


The system is based upon Emerson’s AMS Optimizer product and provides an off-line model and optimizer of the Moerdijk olefins plant.

In addition to predicting the optimal values for the plant setpoints (approximately 100 variables), the system determines the best combination of feedstocks and furnaces based upon the current furnace and feedstock availability.

Plant technologists use the system to evaluate the current plant operation and to investigate the benefits which could be obtained from changes in feedstock or operating philosophy.

Following the success of the first stage of the project Emerson undertook a second stage. This involved an increase in the scope of the optimizer to include additional units both at Moerdijk and Pernis sites.

The system is in use at the Moerdijk site for day-to-day plant operations and at the Pernis site, primarily for longer term studies.

The system comprises the following components:
Model for process simulation and evaluation of plant energy costs
Setpoint optimizer to calculate optimal process setpoints
Mixed integer selection optimizer to determine the optimal furnace feedstock
Model updating to tune furnace models to match current plant performance

* Exact value calculated at Nfl 3M per year. This figure has been converted to US Dollars following the change of the Nfl to the Euro.

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  Shell Nederland Chemie, Moerdijk, Netherlands
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Last Updated 01/25/07


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