- Process Engineering
- Aspen Acol+™
- Aspen Adsim®
- Aspen BatchCAD™
- Aspen Batch Plus®
- Aspen BatchSep™
- Aspen Chromatography®
- Aspen Custom Modeler®
- Aspen Dynamics®
- Aspen FiredHeater™
- Aspen FLARENET™
- Aspen FRAN™
- Aspen HTFS Research Network™
- Aspen HYSYS®
- Aspen HYSYS Amines™
- Aspen HYSYS Crude™
- Aspen HYSYS Dynamics™
- Aspen HYSYS OLGAS™
- Aspen HYSYS PIPESYS™
- Aspen HYSYS Upstream™
- Aspen HX-Net®
- Aspen Icarus Process Evaluator™
- Aspen Icarus Project Manager™
- Aspen Kbase™
- Aspen Muse™
- Aspen Model Runner™
- Aspen Plate+™
- Aspen Plus®
- Aspen Polymers Plus®
- Aspen Process Manual™
- Aspen Process Tools™
- Aspen RateSep™
- Aspen RefSYS™
- Aspen RefSYS Cat Cracker™
- Aspen RefSYS Hydrocracker™
- Aspen RefSYS Reformer™
- Aspen Simulation Workbook™
- Aspen Tasc+™
- Aspen Teams™
- Aspen Zyqad™
- Advanced Process Control
- Planning & Scheduling
- Supply & Distribution
- Production Management & Execution
- Aspen Audit & Compliance Manager™
- Aspen Batch.21™
- Aspen Cim-IO™
- Aspen Compliance.21™
- Aspen eBRS™
- Aspen Golden Batch Profiler™
- Aspen InfoPlus.21®
- Aspen Integration Infrastructure™
- Aspen Operations Domain Model™
- Aspen OpsKPI™
- Aspen Process Explorer™
- Aspen Role-Based Visualization™
- Aspen Utilities Operations™
- Aspen Utilities Planner™
- Aspen Q Server™
- Aspen Web.21™
Aspen Apollo™
Non-linear model-predictive controller
Aspen Apollo is a non-linear, multi-variable model-predictive controller capable of full automation and dynamic optimization of product-grade transitions. It uses a combination of simple, first-principle models (general equations) in conjunction with non-linear approximation technology that can be safely used directly within a controller. Aspen Apollo is a core element of AspenTech’s aspenONE™ Advanced Process Control applications.
Features
- Full non-linear model-predictive control: Supports dynamic and steady state, as well as interacting nonlinearities.
- Reduced modeling complexity: Captures all relationships in a single model per controlled variable.
- All components of the solution reference the same model. Models are gain, time-constant, and delay-type models.
- State-space model formulation features Extended Kalman Filter for unmeasured disturbance handling.
- Requires little or no step testing.
- Highly accurate models, reliable process gain profiles: Eliminates reliance on lab feedback during transitions.
- Constraint ranking: Allows different variables to be ranked for targets and limits so that under certain conditions, the optimizer will focus on higher ranked constraints first.
- Dead time and dynamics: Supports independent dead-time alignment for each pair of relationships, as well as general state space models and parametric dynamics.
- Guaranteed gain and extrapolation: Ensures that bounded derivative network gains will be within specified bounds; models extrapolate sensibly outside data in existing operating regions.
- Variable dynamics support: Supports variable dynamics and dead times; model dynamics can be adjusted online in real-time.
- Gain constrained dynamics: Provides accurate modeling of non-linear gains across the entire operating space.
- Ease of use: Implements interfaces designed by operators for operators.
- Interactive graphical simulation environment: Simulates open loop and closed loop performance, helping you validate controller tuning including move plan, optimization, and unmeasured disturbance rejection.
Benefits
- Full automation and optimization of complex-grade transition strategies
- Easily model multiple catalysts and donors in a single model
- Faster grade transitions
- Reduced maintenance compared to multiple model per CV designs
- Robust solution (a single model per CV eliminates model conflict problems associated with controllers where the inferential model is different to the control model)
Need Help?
Contact Us
Need Support?
Please visit the AspenTech Support site.
Upcoming Events
P&S for Refining & Olefins Users Conference
Oct 22-26, 2007 - Istanbul, Turkey