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Finding good models for model-based control and optimization Paul Van den Hof Okko Bosgra Delft Center for Systems and Control 17 July 2007 Delft Center for Systems and Control 1 The goal Develop tools for supporting economically optimal operation and development of reservoirs on the basis of • plant models of dynamical behaviour, and • observations / measurements of relevant phenomena (pressures, temperatures, flows, production data, seismics) Manipulated variables include: • Valve / production settings (continuous) • Well locations and investments (discrete) Main point 2 Delft Center for Systems and Control Contents • Setting and basic ingredients of the problem • Three relevant modelling issues: • Estimation of physical parameters • Models for filtering/control/optimization • Handling model uncertainty • Conclusions 3 Delft Center for Systems and Control Closed-loop Reservoir Management management, storage, transport economic performance criteria disturbances valve settings reservoir model reservoir actual flow rates, seismics... optimization update state estimation reservoir model - + gain 4 Delft Center for Systems and Control Two roles of reservoir models management, storage, transport Estimation Prediction economic performance disturbances criteria reservoir model actual flow rates, seismics... valve settings reservoir optimization update disturbance + state estimation past present reservoir model future - + gain • Reservoir model used for two distinct tasks: state estimation and prediction. 5 Delft Center for Systems and Control The basic ingredients • Optimal economic operation Balancing short term production targets and long-term reservoir conditions requires accurate models of both phenomena (including quantifying their uncertainty) and performance criteria with constraint handling 6 Delft Center for Systems and Control The basic ingredients • Dynamic models Starting from reservoir models: • Uncertain (continuous as well as discrete), large scale, nonlinear and hard to validate • Saturations are important states that determine long term reservoir conditions (model predictions) • State estimation and parameter estimation (permeabilities) have their own role 7 Delft Center for Systems and Control The basic ingredients • Optimization Gradient-based optimization over inputs, in shrinking horizon implementation Starting from: initial state pdf initial parameter pdf adjoint-based optimization Point of attention: constraint handling (inputs/states) 8 Delft Center for Systems and Control Hierachy of decision levels Reservoir optimization Process control market scheduling day yrs field RTO plant optimization hrs wks well and reservoir MPC advanced control min hrs/day production system PID basic control process sec sec base control layer 9 Delft Center for Systems and Control Points of attention in modelling • How to find the right physics? • Goal oriented modelling • Handling model uncertainty 10 Delft Center for Systems and Control Parameter and state estimation in data reconciliation saturations, pressures e.g. permeabilities Model-based state estimation: past data state update initial state 11 Delft Center for Systems and Control Parameter and state estimation in data reconciliation If parameters are unknown, they can be estimated by incorporating them into the state vector: past data state/parameter update initial state/parameter Can everything that you do not know be estimated? 12 Delft Center for Systems and Control In case of large-scale parameter vector: • Singular covariance matrix (data not sufficiently informative) • Parameters are updated only in directions where data contains information Result: data-based estimation; result and reliability is crucially dependent on initial state/model 13 Delft Center for Systems and Control Parameter estimation in identification Parameter estimation by applying LS/ML criterion to (linearized) model prediction errors e H0(q) v u G0(q) G(q,) e.g. are parameters that describe permeabilities + + - y + presumed data generating system predictor model H(q,)-1 (t) 14 Delft Center for Systems and Control Starting from (linearized) state space form: the model dynamics is represented in its i/o transfer function form: with the shift operator: 15 Delft Center for Systems and Control Principle problem of physical model structures Different might lead to the same dynamic models This points to a lack of structural identifiability There does not exist experimental data that can solve this! Solutions: • Apply regularization (additional penalty term on criterion) to enforce a unique solution (does not guarantee a sensible solution for ) • Find (identifiable) parametrization of reduced dimension 16 Delft Center for Systems and Control Structural identifiability A model structure is locally (i/o) identifiable at if for any two parameters in the neighbourhood of it holds that At a particular point the identifiable subspace of can be computed! This leads to a map with See presentation Jorn van Doren (wednesday) 17 Delft Center for Systems and Control Observations • Local estimate is required for analyzing identifiability. This “relates” to the initial estimate in data-assimilation. • Measure of weight for the relevance of particular directions can be adjusted. • Besides identifiability, finding low-dimensional parametrizatons for the permeability field is a challenge! (rather than “identify everything from data”) • Once the parametrization is chosen, input/experiment design can help in identifying the most relevant directions. 18 Delft Center for Systems and Control Points of attention in modelling • How to find the right physics? • Goal oriented modelling • Handling model uncertainty 19 Delft Center for Systems and Control Goal oriented modelling Well addressed in literature: “identification for control” Identify reduced order model from i/o data to optimize the closed-loop transfer: disturbance disturbance output input process Identification Feedback control system reference input + output controller process - Feedback Feedback control control system system 20 Delft Center for Systems and Control Some general rules for feedback control: • For tracking / disturbance rejection problems: • low-frequent model behaviour usually dominated by (integrating) controller • best models are obtained from closed-loop experiments (similar to intended application) disturbance disturbance output input process Identification Feedback control system reference input + output controller process - Feedback Feedback control control system system 21 Delft Center for Systems and Control Identification for filtering / optimization Question: are these relevant and feasible problems? 1. Find the model that leads to the best possible state estimate of the relevant states (saturations, pressures) 2. Find the model that leads to the best possible future production prediction Problems might include: generation of experimental data 22 Delft Center for Systems and Control Steps from data to prediction prior knowledge + production data to be optimized • Shows dual role of model: state estimation and long term prediction Typical for the reservoir-situation: • current data only shows (linearized) dynamics of current reservoir situation (oil/water-front) • future scenario’s require physical model (permeabilities) 23 Delft Center for Systems and Control Steps from data to prediction prior knowledge + production data observability to be optimized controllability Relevant phenomena for assessing the dominant subspaces of the state space [See presentation of Maarten Zandvliet, Wednesday] 24 Delft Center for Systems and Control Points of attention in modelling • How to find the right physics? • Goal oriented modelling • Handling model uncertainty 25 Delft Center for Systems and Control Handling model uncertainty prior knowledge + production data to be optimized + uncertainty + uncertainty + uncertainty Sources: • Different geological scenarios • Model deficiencies • ………. 26 Delft Center for Systems and Control First results (Gijs van Essen en Maarten Zandvliet) Robust performance (open-loop strategy) based on 100 realizations/scenario’s 27 Delft Center for Systems and Control Challenge for next step: “learn” the most/less likely scenario’s during closed-loop operation 28 Delft Center for Systems and Control Conclusions • Basic methods and tools have been set, but there remain important and challenging questions, as e.g.: • Complexity reduction of the physical models: limit attention to the esssentials • Structurally incorporate the role of uncertainties in modelling and optimization • Major steps to be made to discrete-type optimization/decisions: e.g. well drilling • Take account of all time scales (constraint handling) 29 Delft Center for Systems and Control