Multivariate process chart to control a process to produce a chemical, pharmaceutical, biopharmaceutical and/or biological product
AssigneeSartorius Stedim Data Analytics AB
InventorsMarek Hoehse, Christian Grimm
Life of this patent
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Abstract
Aspects of the application relate to methods, a computer program and a process control device. According to one aspect, a computer-implemented method for determining a multivariate process chart is provided. The multivariate process chart is to be used to control a process to produce a chemical, pharmaceutical, biopharmaceutical and/or biological product. The multivariate process chart includes a first trajectory, an upper limit for the first trajectory and a lower limit for the first trajectory.
Claims15
A computer-implemented method for determining a multivariate process chart, the multivariate process chart to be used to control a process to produce a chemical, pharmaceutical, biopharmaceutical and/or biological product, the multivariate process chart including a first trajectory, an upper limit for the first trajectory and a lower limit for the first trajectory, the method comprising:
- providing a plurality of first-scale vessels, each of the first-scale vessels containing fluid for producing the product;
- receiving, by a first process control device, process parameters, the process parameters including process parameters to be controlled and process parameters to be measured;
- controlling, by the first process control device and at least partly in parallel, the process in each of the first-scale vessels, wherein the first process control device is in continuous operation in order to control each of the first-scale vessels;
- periodically determining, at least in part by the first process control device, process parameter values for the process parameters from the fluid ineach of the first-scale vessels;
- defining groups of the process parameter values according to a common characteristic, wherein each of the groups includes process parameter values determined from multiple ones of the first-scale vessels, wherein the groups of process parameter values are defined according to the times at which the process parameter values were determined;
- determining at least one statistically representative value for each of the groups of process parameter values, such that each of the groups of the process parameter values has a different corresponding statistically representative value;
- establishing the first trajectory from the statistically representative values;
- and
- determining the upper limit and the lower limit based on a measure of variation within each group,
- wherein the method further includes selectively excluding process parameter values determined from respective ones of the first-scale vessels in order to identify remaining process parameter values, wherein the groups of the process parameter values consist of the remaining process parameter values, and
- wherein the remaining process parameter values are identified when at least one of the following criteria applies:
- i. process parameter values determined from one of the respective ones of the first-scale vessels are identified as outliers in comparison to process parameter values determined from the other first-scale vessels,
- ii. at least one of the process parameters is identified as a critical process parameter, and values of the critical process parameter determined from one of the respective ones of the first-scale vessels are outside an accepted range,
- iii. process output values determined from one of the respective ones of the first-scale vessels are outside an accepted range;
- iv. a predicted first trajectory for one of the respective ones of the first-scale vessels is more than a specified distance from a golden batch trajectory for the first-scale vessels or a nearest neighbor of the respective one of the first-scale vessels;
- and
- v. a multivariate score for one of the respective ones of the first-scale vessels is outside an accepted range or more than a specified distance from the golden batch trajectory, wherein the multivariate score is derived from process parameter values and/or process output values of the respective one of the first-scale vessels.
A computer-implemented method for controlling a process to produce a chemical, pharmaceutical, biopharmaceutical and/or biological product using a multivariate process chart, the method comprising:
- determining the multivariate process chart that includes a first trajectory, an upper limit for the first trajectory and a lower limit for the first trajectory by:
- providing a plurality of first-scale vessels, each of the first-scale vessels containing fluid for producing the product;
- receiving, by a first process control device, process parameters, the process parameters including process parameters to be controlled and process parameters to be measured;
- controlling, by the first process control device and at least partly in parallel, the process in each of the first-scale vessels, wherein the first process control device is in continuous operation in order to control each of the first-scale vessels;
- periodically determining, at least in part by the first process control device, process parameter values for the process parameters from the fluid in each of the first-scale vessels;
- defining groups of the process parameter values according to a common characteristic, wherein each of the groups includes process parametervalues determined from multiple ones of the first-scale vessels, wherein the groups of process parameter values are defined according to the times at which the process parameter values were determined;
- determining at least one statistically representative value for each of the groups of process parameter values, such that each of the groups of the process parameter values has a different corresponding statistically representative value;
- establishing the first trajectory from the statistically representative values;
- determining the upper limit and the lower limit based on a measure of variation within each group;
- providing at least one second-scale vessel, the second-scale vessel containing fluid for producing the product, wherein a size of the second-scale vessel differs by at least one order of magnitude from a size of one of the first-scale vessels;
- receiving, by a second process control device, the process parameters;
- carrying out, by the second process control device, the following steps:
- controlling the process in the second-scale vessel;
- periodically determining process parameter values for the process parameters from the fluid in the second-scale vessel;
- estimating an actual trajectory of the process from the process parameter values;
- and
- when a deviation of the actual trajectory from the first trajectory exceeds the upper limit or the lower limit, controlling the process to correct the deviation, thereby influencing at least one of the process parameters.
Dependencies are inferred from the claim text.