Hardware integration
The most critical step of integration is to ensure that DeltaV can communicate with the individual process units using some suitable protocols. Therefore it is important to pick a set of protocols that the DeltaV cards can all use at once, so that each process unit can talk at least one of those protocols using one of those hardware connectors. Once the protocols are fixed, reading the data from the equipment is relatively straightforward.
Embodiment 2: In addition to the control loops for individual units and sensors presented above for embodiment 1, the dry granulation testbed is being installed at Purdue. The manipulated and controlled variables of roller compactor are summarized as follows:
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Manipulated variables
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Controlled variables
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Roller Compactor
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Ribbon density
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Feed screw speed
Roll pressure
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Control strategies
The planned control strategy for the feeder/blender/roller compactor is a cascade control design focusing on the feeder group and the roller compactor.
· The planned control strategy is to use MPC on the roller compactor, based on the work already done as part of Project D4 by Hsu et al. The aim is to simultaneously control ribbon density and roll gap by simultaneously manipulating the feed screw speed and the hydraulic pressure. Currently the roller compactor is being run in open loop for the ribbon characterization experiments. The roller compactor also has in-built PID control to maintain roll gap which has been used for ribbon characterization.
· The ratios of the API and excipient feed rates will be controlled by a local master-slave control system. The feeders have in-built control systems for manipulating the feed screw speed for a set feed rate. The ratio control will vary the setpoint on one feeder to keep it within a constant ratio of the feed rate of another feeder, should the feed rate vary for any reason.
· The blender will have only minimal control, focusing only on the rpm. Other aspects of the blender are essentially open loop, with feedback achieved by the overall control cascade.
Sensors
· Scales on the feeders
· NIR – powder concentration on the continuous mixer
· NIR – ribbon density on the roller compactor. Offline measurements indicate good correlation between NIR spectrum slope and the ribbon density. The online NIR monitoring is under development.
· Characterization of ribbon properties in the middle API loading region: The ribbon densities and tensile strength have been characterized under different formulations and different operating conditions to suggest the appropriate operating region for continuous ribbon manufacturing. Feeder and blender selection and installation: Schenck AccuRate feeders are selected as the feeding system to be consistent with Embodiment 1. The feeders have been calibrated and verified to convey excipient and API at the different flowrate setpoints. The motor and controller have been selected to be compatible with the body donated by Gericke. The installation of blender is undergoing and will be complete at the end of February. Hardware integration: Set up communication between DeltaV control system and individual equipment. The Alexanderwerk roller compactor has been integrated with DeltaV through Ethernet IP. The Schenck AccuRate feeders had been integrated using Ethernet IP as well, however communication proved problematic due to incompatible master/slave settings on the feeder cards and the VIM card used by DeltaV. It was therefore decided to switch the protocol to Profibus, which eliminates the master/slave problem. The cards have been replaced, and commisioning is in progress. The blender motor controller was selected to use Profibus as well to synergize with the feeders.
F. Timed Deliverables
For the period 1/1/2009 – 6/30/2009, activities on Embodiment 1 will concentrate on installing and linking DeltaV and the sensors, and setting up the PAT software. Development of Embodiment 2 will focus on interconnecting the main hardware components in order to assemble the integrated line, and expanding the integration with DeltaV, Pope, and the ABB PAT software. The timed deliverables for TB 1 for this six-month period, which were presented in Section 2.2.4, include the following:
· Phase I of embodiment 2 system (feeders, blender, roller compactor) to be completed 4/2/2009.
· DeltaV control system at Rutgers installed and operational by 4/2/2009 (project 1.2)
· ABB multichannel analyzer, NIR and Raman sensors selected, installed, and interfaced by 6/1/2009 (project 1.1)
· ABB PAT software installed and interfaced by 6/1/2009 (project 1.2)
· Interface POPE/MPC system with roller compactor system by 3/30/2009 (project 1.3),
· Test RTO & EEM for TB1 simulations by 3/30/2009 and integrate process control for embodiment 2 (including startup/shutdown) by 6/30/2009 (project 1.4)
· Reduced order model for integrated operation of feeders and mixer completed by 6/30/2009 (project 1.5)
· Characterization of effects of feed frame operational parameters on particle size distribution and hydrophobicity of blends completed for the current case study by 6/30/2009 (project 2.1).
· Dynamic behavior of the mixer characterized for the present case study (project 2.2) finalized by 6/30/2009
· Major effects of composition, shear rate, strain, compression force, and compression speed on tablet content uniformity, hardness, and dissolution characterized for the current case study by 6/30/2009 (project 2.3).
· Measurement and modeling of particle adhesion to surfaces, specifally accounting for particle nonuniformities and roughness, as well as substrate roughness (project 3.1).
· Preliminary measurements and models of effect of relative humidity on particle adhesion (project 3.1).
If the proposed research program reorganization is approved, deliverables after 7/1/2009 refer to the new project line-up. Major components of research activities planned for the next three years include:
· The main focus will fall on the closed loop operation of both continuous lines. This includes the full implementation and integration of sensing and control systems (projects D1, D2 and D4) ) and implementation of exceptional events management and real time optimization on both lines.
· NIR sensing seems the most promising component for blend homogeneity and density. The working hypothesis is that the response surface is of low dimensionality and that these variables will provide sufficient control of the process. If this Hypothesis proves to be incorrect, additional sensing method will be implemented. Negotiations are underway with multiple companies, including ABB and VTT for the supply of sensors (project D1).
· Efforts will continue in the characterization and understanding of the multivariate relationship between inputs (raw materials properties, powder composition, shear/strain, compression force, compression speed), intermediate material properties (blend homogeneity, cohesion, density, blend and tablet hydrophobicity), and “finished product” responses (tablet weight variability, hardness, dissolution, drug content uniformity). A large study already under way will be continued (project D5).
· The informatics framework developed in Project D3 will be customized and expanded in order to provide an integrated modeling platform for the Test Bed.
· Commissioning of the integrated embodiment 2 line will be completed. The line will be operated in open and closed loop with extreme events to collect data for the validating extreme events management system ) and implementation of exceptional events management and real time optimization on both lines.
· The emphasis of dynamic experiments for validation of process control, EEM and RTO strategies will move from changes in process parameters to feed formulation changes eg. variability in excipient properties.
· The development and improvement of both detailed physics-based models and coarse models for the design and scaling of each process involved in the continuous tablet manufacturing will continue. Steady state experiments using test bed 1 will play a major role in validating and continuously improving these models. These models will further the understanding of the phenomena underlying the relationships between material mechanical and micromeritic properties, operating conditions and product characteristics as well as facilitate the system control (projects B1, B2, B4, and B5).
· Activities in project C2 will continue to expand the database of powder flow properties as a function of composition and strain. Characterizations of feeders and feed frames will continue in project B1, expanding available information regarding the operation of powder feeding equipment.
· Project B2 will complete the basic characterization of mixing performance in the “Niro 2” and the Gericke mixer using experiments, DEM and statistical models, and PEPT experiments that will be performed in the UK in collaboration with Professor Jonathan Seville.
· Projects B4, C3 and C4 will expand efforts in modeling of the compression process, focusing on understanding the effect of blend properties and compression parameters on tablet microstructure and performance.
· Test bed 1 will also provide the platform for testing modified equipment designs that result from the fundamental understanding and modeling that is occurring in thrust B (B1, B2, B4, B5).
· An extension to test bed 1 to include continuous wet granulation in the final year of this period will be considered.
For the period 7/1/2009 – 6/30/2010, activities at Rutgers will concentrate primarily on exploring the performance space for low drug concentration (1-5 %), examining the effect of API (APAP and others TBD), lubricant (MgSt), SIO2, and excipient grades (Avicels 101, 102, 200, Lactose Fast flow, milled lactose), examining product structure, determining dissolution performance. At Purdue, the focus will be on exploring the performance space for the largest drug concentration (60-100%). A key material issue to be explored in detail is the joint size/density/composition distribution of the dry-granulated material and its impact on product performance. Timed deliverables for this period include:
· Methods for modifying flow properties and achieve effective continuous feeding of APIs will be implemented (projects B1 and C2)
· Mixing performance and effects of strain for minor ingredients (lubricant, and SiO2) characterized (project B2)
· Reduced order model of integrated feeders and mixer for all ingredients available (Project D5)
· Powder compaction models including inter-particle deformation and bonding experimentally validated and calibrated (Projects B4, B5, C4).
· Stress distributions during roll compaction measured directly on the test bed for a range of conditions to validate FEM based design model (B4)
· On line sensing of ribbon density and cross ribbon density variability installed and validated for the Purdue embodiment (B4, D1)
· Reduced order models for the integrated operation of the tablet press and roll compactor implemented (Project B5, B4).
· On-line sensing of tablet properties including tablet weight, thickness and surface composition implemented (Project D1).
· Feed frame operation characterization and investigation of operating parameters on powder flow properties (Project B1).
· Measurement, modeling and integration of effects of individual particle chemical and mechanical properties on particle-particle and particle-substrate interactions, including effects of relative humidity and inferences for powder flow and processing.
· Tablet mechanical properties and internal structure characterization and correlation to powder composition and process parameters (Projects C3, C4, C5).
· Implementation of NIR chemical imaging and development of novel Raman imaging techniques to further understand the structure of the composites under development.(July,2009)
· Initiate on-line Raman monitoring using fiber optic probes. (July, 2009)
· Methods for on-line monitoring of powder density. (July, 2009)
· Set up Raman spectrometer to study formation of polymorphs in as-received and processed drug powders in the
Tera Hertz region below 150 cm-1. (July, 2010)
· Prepare accurate density and moisture standards and measure dielectric properties. Use X-ray tomography to measure density variations in samples. Compare reflection and transmission methods for measuring complex dielectric properties of powder density standards. Complete initial test of microwave reflection probe on fluidize bed or ribbon process to measure density. (July 2010)
· Evaluate the capability of SORS (Surface Offset Raman Spectroscopy) imaging and photon migration for measuring powder and roller compact bulk density. (July 201)0
· Complete simultaneous moisture content and density measurements by microwave reflection and transmission methods on fluidize bed and ribbon processes. (July 2010)
· Expand spectroscopic methods for porosity to assess the relationship between shear forces and porosity for multi-component compacts prepared under unrestricted geometry as in roller compaction. (2011)
· Quantitatively compare multivariate hyperspectral imaging (MHI) and CCD based micro-Raman imaging methods (2011).
· Full integration of process components, sensors, and informatics completed (project D1, D2 and D4)
· Failure modes for low API concentration identified. Control actions needed to prevent or overcome failures identified and tested (project D3).
· Substantial validation for EEM and RTO strategies on both lines (Project D4)
· Process and composition design space for low-content and high drug content scenarios determined (Project D5)
For the period 7/1/2010 – 6/30/2011, activities both at Rutgers and Purdue will concentrate primarily on exploring (a) modifications to equipment design to improve performance, and (b) the performance space for intermediate drug concentrations (20-40%). This will allow us to compare and explore relative benefits of Roller Compacted vs. Directly Compressed formulations. Most key deliverables during this period are similar to those listed above for the previous year. A few necessary additions include:
· Modification to the feed system for the roll compactor to improve cross ribbon density distribution and validation of the system using embodiment
· Mixing performance for larger API concentrations will be characterized. Feeder/mixer model will be updated (projects B1 and B2).
· Powder compaction models for larger API concentrations will be expanded to include roller-compacted materials (projects B4, B5, and C4).
· Failure modes for intermediate API concentration identified. Control actions needed to prevent or overcome failures identified and tested (project D3).
· Process and composition design space for low-content scenario determined (project D3).
· Application of designer particles with physical, mechanical, and chemical properties selected based on first principles models of relationship between particle and substrate properties and powder behavior. Validation of relationships between particle properties and population behavior.
· Scoping study for developing a expansion of test bed 1 to incorporate continuous wet granulation.
Finally, for the period 7/1/2011 and 7/1/2012, activities will focused on more advanced structured materials - blends containing nanoparticles and nanocoatings, possibly with encapsulated biomolecules. If a decision is made to expand the test bed to include wet granulation, this will be a made focus for 2011/2012. Timed deliverables for this period will be provided at a later date.