US20020019722A1 - On-line calibration process - Google Patents
On-line calibration process Download PDFInfo
- Publication number
- US20020019722A1 US20020019722A1 US09/892,417 US89241701A US2002019722A1 US 20020019722 A1 US20020019722 A1 US 20020019722A1 US 89241701 A US89241701 A US 89241701A US 2002019722 A1 US2002019722 A1 US 2002019722A1
- Authority
- US
- United States
- Prior art keywords
- prediction
- deviation
- model
- mathematical model
- kalman filter
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- 238000000034 method Methods 0.000 title claims abstract description 80
- 230000008569 process Effects 0.000 title claims abstract description 48
- 238000005259 measurement Methods 0.000 claims abstract description 21
- 238000013178 mathematical model Methods 0.000 claims abstract description 19
- 230000006870 function Effects 0.000 claims abstract description 13
- 238000012545 processing Methods 0.000 claims abstract description 6
- 238000012546 transfer Methods 0.000 claims abstract description 6
- 238000013528 artificial neural network Methods 0.000 claims description 2
- 238000012417 linear regression Methods 0.000 claims description 2
- FGUUSXIOTUKUDN-IBGZPJMESA-N C1(=CC=CC=C1)N1C2=C(NC([C@H](C1)NC=1OC(=NN=1)C1=CC=CC=C1)=O)C=CC=C2 Chemical compound C1(=CC=CC=C1)N1C2=C(NC([C@H](C1)NC=1OC(=NN=1)C1=CC=CC=C1)=O)C=CC=C2 FGUUSXIOTUKUDN-IBGZPJMESA-N 0.000 claims 2
- 238000004364 calculation method Methods 0.000 description 3
- 238000012369 In process control Methods 0.000 description 2
- 238000010965 in-process control Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 238000003908 quality control method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 238000005309 stochastic process Methods 0.000 description 1
Classifications
-
- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05B—CONTROL OR REGULATING SYSTEMS IN GENERAL; FUNCTIONAL ELEMENTS OF SUCH SYSTEMS; MONITORING OR TESTING ARRANGEMENTS FOR SUCH SYSTEMS OR ELEMENTS
- G05B13/00—Adaptive control systems, i.e. systems automatically adjusting themselves to have a performance which is optimum according to some preassigned criterion
- G05B13/02—Adaptive control systems, i.e. systems automatically adjusting themselves to have a performance which is optimum according to some preassigned criterion electric
- G05B13/0265—Adaptive control systems, i.e. systems automatically adjusting themselves to have a performance which is optimum according to some preassigned criterion electric the criterion being a learning criterion
- G05B13/027—Adaptive control systems, i.e. systems automatically adjusting themselves to have a performance which is optimum according to some preassigned criterion electric the criterion being a learning criterion using neural networks only
-
- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05B—CONTROL OR REGULATING SYSTEMS IN GENERAL; FUNCTIONAL ELEMENTS OF SUCH SYSTEMS; MONITORING OR TESTING ARRANGEMENTS FOR SUCH SYSTEMS OR ELEMENTS
- G05B13/00—Adaptive control systems, i.e. systems automatically adjusting themselves to have a performance which is optimum according to some preassigned criterion
- G05B13/02—Adaptive control systems, i.e. systems automatically adjusting themselves to have a performance which is optimum according to some preassigned criterion electric
-
- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05B—CONTROL OR REGULATING SYSTEMS IN GENERAL; FUNCTIONAL ELEMENTS OF SUCH SYSTEMS; MONITORING OR TESTING ARRANGEMENTS FOR SUCH SYSTEMS OR ELEMENTS
- G05B17/00—Systems involving the use of models or simulators of said systems
- G05B17/02—Systems involving the use of models or simulators of said systems electric
Definitions
- the present invention relates to an automatic online calibration of input/output models.
- QE Quality Estimators
- QE's are usually identified from collected process data.
- a QE has to be calibrated using historic quality measurements, which can be taken on-line or off-line depending on the type of process and/or the type of measurement envisaged, so as to minimize, or preferably avoid, any drift in the predicted quality.
- QE's are preferably used in situations which allow rather infrequent and/or delayed measurements of product quality. This may be the case when, for instance, the amount of time needed to produce the measured value is rather long or when the method is relatively costly.
- the Robust Quality Estimator (RQE) provides a more accurate and robust quality prediction which improves the performance of any quality control scheme in which it is applied. For instance, it improves the performance of a linear model predictive controller when the process is such that the steady-state gains and/or the dynamics (such as the deadtime) between the manipulated variables and the controlled quality are varying in an unpredictable manner within certain identified boundaries. Moreover, is can also be used to facilitate closed-loop control of any process variable with a difficult dynamic behaviour.
- the present invention therefore relates to a method for automatic on-line calibration of process models for real-time prediction of process quality from raw process measurements which method comprises the steps of collecting raw process data, processing data collected through a mathematical model to obtain a prediction of the quality, processing this prediction through two independent dynamic transfer functions thus creating two intermediate signals, storing the two intermediate signals obtained as a function of time in history, retrieving, at the time of a real and validated measurement of the quality, from the history the absolute minimum and maximum values of the two intermediate signals in the time period corresponding to a minimum and maximum specified deadtime, which values define the minimum and maximum prediction possible, calculating the deviation as being the difference between the real and validated measurement and the area encompassed between the minimum and maximum prediction possible as obtained, and repeating these steps if the absolute value of the deviation obtained is zero, or, if the absolute value of the deviation obtained is larger than zero, incorporating the deviation into the process model and repeating the steps.
- the collection of raw process data to be used in the method according to the present invention can be carried out by methods known in the art. It is customary in process control technology to measure data at a number of points over a period of time. For instance, in refining operations, operating parameters such as temperature, pressure and flow are normally measured at frequent intervals, or even in a continuous manner and they can be stored and processed in many ways as is known to those skilled in the art.
- An essential step in the method for automatic on-line calibration is the calculation of the minimum and maximum prediction possible at the time of the real and validated measurement(s) of the quality.
- This can be achieved by applying two independent dynamic transfer functions (so-called uncertain dynamics) to the undelayed real time, thus creating two (independent) intermediate signals.
- uncertain dynamics independent dynamic transfer functions
- These intermediate signals are stored as a function of time in history. This will result in essence in an (uncertainty) area in which the actual process response should be placed and which will become very narrow when reaching the steady-state situation. It is also possible that the uncertainty area is reduced to a line corresponding to the event in which the two independent dynamic transfer functions are identical.
- the so-called minimum and maximum prediction possible are obtained by calculating from the history the absolute minimum and maximum values of these two intermediate signals in the time period corresponding to a minimum and maximum specified deadtime.
- the area Before reaching the steady-state situation, the area can be very wide.
- the state of the art systems will either only calibrate during steady-state or have the risk of making a false calibration in case the real and validated measurement(s) of the quality is within the above mentioned area.
- the method according to the present invention is specifically designed to calibrate only when the real and validated measurement(s) of the quality are outside the uncertainty area, thus preventing instabilities in closed-loop.
- the calibration process is carried out by calculating the deviation (so-called prediction error) as being the distance between the real and validated measurement and the area encompassed between the minimum and maximum prediction possible as obtained from the earlier calculation.
- the deviation found will not be used as further input in the calibration process but the system will continue by repeating the steps carried out up till now as there is no need to refine the system. If, however, the deviation as calculated shows that the absolute value of the deviation is larger than zero, the deviation obtained will be incorporated into the process model and the previous steps will be repeated. The net result will be the generation of a modified, more precise, prediction model which will then serve as the basis for further modifications depending on the level of deviations being observed during the course of the calibrating process.
- Kalman filter When incorporation of the allowed deviation into the process model is envisaged with the use of a Kalman filter the result will be that the deviation can be incorporated into the mathematical model by adjusting its linear parameters thereby updating the prediction band and improving the mathematical model.
- the use of a Kalman filter is well known in the art of process control operations. Reference is made in this respect to “Stochastic Processes and Filtering Theory” by Jazwinski (Academic Press, Mathematics and Science and Engineering, Vol. 64, 1970). Since Kalman filters are, in essence, optimal stochastic filters, they also filter out, or even eliminate, the noise on the measured quality which makes them very suitable for use in the method according to the present invention.
- Kalman filters is not limited to calibration operations which are carried out under non steady-state conditions as it is equally capable of providing useful information when a process is being operated under steady-state conditions. Under such conditions it has the additional advantage that it will reduce the prediction error in the future which makes the QE part of a learning system which is upgrading itself when applied in practice.
- the calibration process as described in the present invention can be extrapolated for robust multivariable predictive controllers to cover uncertain dynamics in the control model for all the transfer functions between the manipulated variables and the controlled variables.
Landscapes
- Engineering & Computer Science (AREA)
- Artificial Intelligence (AREA)
- Physics & Mathematics (AREA)
- Automation & Control Theory (AREA)
- Evolutionary Computation (AREA)
- General Physics & Mathematics (AREA)
- Computer Vision & Pattern Recognition (AREA)
- Software Systems (AREA)
- Medical Informatics (AREA)
- Health & Medical Sciences (AREA)
- Feedback Control In General (AREA)
- Management, Administration, Business Operations System, And Electronic Commerce (AREA)
- Testing, Inspecting, Measuring Of Stereoscopic Televisions And Televisions (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP00306148.8 | 2000-07-19 | ||
| EP00306148 | 2000-07-19 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20020019722A1 true US20020019722A1 (en) | 2002-02-14 |
Family
ID=8173132
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US09/892,417 Abandoned US20020019722A1 (en) | 2000-07-19 | 2001-06-27 | On-line calibration process |
| US10/333,446 Expired - Lifetime US7359830B2 (en) | 2000-07-19 | 2001-07-17 | Method for automatic on-line calibration of a process model |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US10/333,446 Expired - Lifetime US7359830B2 (en) | 2000-07-19 | 2001-07-17 | Method for automatic on-line calibration of a process model |
Country Status (10)
| Country | Link |
|---|---|
| US (2) | US20020019722A1 (fr) |
| EP (1) | EP1301832B1 (fr) |
| JP (1) | JP2004510222A (fr) |
| KR (1) | KR100810952B1 (fr) |
| CN (1) | CN1193279C (fr) |
| AU (1) | AU2001289682A1 (fr) |
| CA (1) | CA2418226C (fr) |
| DE (1) | DE60106045T2 (fr) |
| RU (1) | RU2280270C2 (fr) |
| WO (1) | WO2002006905A2 (fr) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20030158680A1 (en) * | 2000-07-19 | 2003-08-21 | Wim Hupkes | On-line calibration process |
| US20130006566A1 (en) * | 2010-07-02 | 2013-01-03 | Idexx Laboratories, Inc. | Automated Calibration Method and System for a Diagnostic Analyzer |
| DE102006045429B4 (de) | 2005-09-30 | 2018-07-19 | Fisher-Rosemount Systems, Inc. | Adaptive, Modellprädiktive Online-Steuerung in einem Prozesssteuerungssystem |
Families Citing this family (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1323336C (zh) * | 2003-12-08 | 2007-06-27 | 西安交通大学 | 设备运行状态数据质量动态检测和保障方法 |
| DE102004028557A1 (de) * | 2004-06-15 | 2006-02-16 | Abb Patent Gmbh | Verfahren und System zur Zustandsbewertung von wenigstens einem Achsgelenk |
| US20050283096A1 (en) * | 2004-06-17 | 2005-12-22 | Bloorview Macmillan Children's Centre, A Corp. Registered Under The Ontario Corporations Act | Apparatus and method for detecting swallowing activity |
| JP4375143B2 (ja) * | 2004-07-06 | 2009-12-02 | 株式会社日立製作所 | 動画像符号化装置 |
| US20060095312A1 (en) * | 2004-10-28 | 2006-05-04 | International Business Machines Corporation | Method, system, and storage medium for using comparisons of empirical system data for testcase and workload profiling |
| US20060156619A1 (en) * | 2004-12-24 | 2006-07-20 | Crawshaw Elizabeth H | Altering properties of fuel compositions |
| EP1674553A1 (fr) * | 2004-12-24 | 2006-06-28 | Shell Internationale Researchmaatschappij B.V. | Modification de propriétés de compositions de combustible. |
| EP1674552A1 (fr) * | 2004-12-24 | 2006-06-28 | Shell Internationale Researchmaatschappij B.V. | Compositions de Combustibles. |
| US7444191B2 (en) | 2005-10-04 | 2008-10-28 | Fisher-Rosemount Systems, Inc. | Process model identification in a process control system |
| US8036760B2 (en) * | 2005-10-04 | 2011-10-11 | Fisher-Rosemount Systems, Inc. | Method and apparatus for intelligent control and monitoring in a process control system |
| US7738975B2 (en) * | 2005-10-04 | 2010-06-15 | Fisher-Rosemount Systems, Inc. | Analytical server integrated in a process control network |
| BRPI0718870A8 (pt) * | 2006-11-07 | 2017-02-07 | Saudi Arabian Oil Co | controle avançado de processo de craqueamento catalítico severo de fluido para maximizar a produção de propileno de uma matéria prima de petróleo |
| US7970482B2 (en) * | 2007-08-09 | 2011-06-28 | Honeywell International Inc. | Method and system for process control |
| US8571696B2 (en) * | 2009-06-10 | 2013-10-29 | Fisher-Rosemount Systems, Inc. | Methods and apparatus to predict process quality in a process control system |
| US9323234B2 (en) | 2009-06-10 | 2016-04-26 | Fisher-Rosemount Systems, Inc. | Predicted fault analysis |
| CN101859103B (zh) * | 2010-06-02 | 2012-07-25 | 清华大学 | 催化裂化反应深度在线计算和自适应非线性预测控制方法 |
| CN102890452B (zh) * | 2012-10-11 | 2014-11-26 | 西北工业大学 | 基于可变测量数最大信息量-可信度准则的飞行器建模方法 |
| CN113358825B (zh) * | 2021-06-02 | 2023-03-24 | 重庆大学 | 一种带同化算法的室内空气质量检测器 |
| CN118550192B (zh) * | 2024-05-15 | 2024-11-29 | 苏州贯龙电磁线有限公司 | 一种导体尺寸在线检测及自动反馈调节系统及方法 |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5646870A (en) * | 1995-02-13 | 1997-07-08 | Advanced Micro Devices, Inc. | Method for setting and adjusting process parameters to maintain acceptable critical dimensions across each die of mass-produced semiconductor wafers |
| US5884685A (en) * | 1995-03-29 | 1999-03-23 | Nippon Steel Corporation | Quality prediction and quality control of continuous-cast steel |
| US5918191A (en) * | 1997-03-11 | 1999-06-29 | Certified Measurements, Inc. | System and method for managing data for an equipment calibration laboratory |
| US6487459B1 (en) * | 1996-05-06 | 2002-11-26 | Pavilion Technologies, Inc. | Method and apparatus for modeling dynamic and steady-state processes for prediction, control and optimization |
| US6532428B1 (en) * | 1999-10-07 | 2003-03-11 | Advanced Micro Devices, Inc. | Method and apparatus for automatic calibration of critical dimension metrology tool |
| US20030158680A1 (en) * | 2000-07-19 | 2003-08-21 | Wim Hupkes | On-line calibration process |
| US6635224B1 (en) * | 1998-10-30 | 2003-10-21 | General Electric Company | Online monitor for polymer processes |
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| SU769496A1 (ru) * | 1978-11-20 | 1980-10-07 | Военный Инженерный Краснознаменный Институт Им. А.Ф.Можайского | Устройство дл контрол динамических систем |
| JPS61248104A (ja) * | 1985-04-26 | 1986-11-05 | Nissan Motor Co Ltd | マニピユレ−タの制御装置 |
| FR2611911B1 (fr) | 1987-02-27 | 1989-06-23 | Bp France | Procede de determination directe d'un indice d'octane |
| RU2042168C1 (ru) * | 1990-05-14 | 1995-08-20 | Акционерное общество открытого типа "Научно-исследовательский технологический институт" | Адаптивная система регулирования процесса контроля на металлорежущем станке |
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| US5814783A (en) * | 1995-02-24 | 1998-09-29 | Board Of Regents, University Of Texas Systems | Method and apparatus for real-time weld-quality control and post-process weld-quality verification for homopolar pulsed welding |
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| RU2146063C1 (ru) * | 1999-04-05 | 2000-02-27 | Кемеровский государственный университет | Способ идентификации линейного объекта |
| EP1111550B1 (fr) * | 1999-12-23 | 2003-08-27 | Abb Ab | Méthode et système pour surveiller le fonctionnement d'une machine isolée |
-
2001
- 2001-06-27 US US09/892,417 patent/US20020019722A1/en not_active Abandoned
- 2001-07-17 US US10/333,446 patent/US7359830B2/en not_active Expired - Lifetime
- 2001-07-17 RU RU2003104831/09A patent/RU2280270C2/ru active
- 2001-07-17 CN CNB01812951XA patent/CN1193279C/zh not_active Expired - Lifetime
- 2001-07-17 CA CA2418226A patent/CA2418226C/fr not_active Expired - Lifetime
- 2001-07-17 DE DE60106045T patent/DE60106045T2/de not_active Expired - Lifetime
- 2001-07-17 JP JP2002512752A patent/JP2004510222A/ja active Pending
- 2001-07-17 WO PCT/EP2001/008288 patent/WO2002006905A2/fr not_active Ceased
- 2001-07-17 AU AU2001289682A patent/AU2001289682A1/en not_active Abandoned
- 2001-07-17 EP EP01969417A patent/EP1301832B1/fr not_active Expired - Lifetime
- 2001-07-17 KR KR1020037000787A patent/KR100810952B1/ko not_active Expired - Lifetime
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5646870A (en) * | 1995-02-13 | 1997-07-08 | Advanced Micro Devices, Inc. | Method for setting and adjusting process parameters to maintain acceptable critical dimensions across each die of mass-produced semiconductor wafers |
| US5655110A (en) * | 1995-02-13 | 1997-08-05 | Advanced Micro Devices, Inc. | Method for setting and adjusting process parameters to maintain acceptable critical dimensions across each die of mass-produced semiconductor wafers |
| US5884685A (en) * | 1995-03-29 | 1999-03-23 | Nippon Steel Corporation | Quality prediction and quality control of continuous-cast steel |
| US6487459B1 (en) * | 1996-05-06 | 2002-11-26 | Pavilion Technologies, Inc. | Method and apparatus for modeling dynamic and steady-state processes for prediction, control and optimization |
| US5918191A (en) * | 1997-03-11 | 1999-06-29 | Certified Measurements, Inc. | System and method for managing data for an equipment calibration laboratory |
| US6635224B1 (en) * | 1998-10-30 | 2003-10-21 | General Electric Company | Online monitor for polymer processes |
| US6532428B1 (en) * | 1999-10-07 | 2003-03-11 | Advanced Micro Devices, Inc. | Method and apparatus for automatic calibration of critical dimension metrology tool |
| US20030158680A1 (en) * | 2000-07-19 | 2003-08-21 | Wim Hupkes | On-line calibration process |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20030158680A1 (en) * | 2000-07-19 | 2003-08-21 | Wim Hupkes | On-line calibration process |
| US7359830B2 (en) * | 2000-07-19 | 2008-04-15 | Shell Oil Company | Method for automatic on-line calibration of a process model |
| DE102006045429B4 (de) | 2005-09-30 | 2018-07-19 | Fisher-Rosemount Systems, Inc. | Adaptive, Modellprädiktive Online-Steuerung in einem Prozesssteuerungssystem |
| US20130006566A1 (en) * | 2010-07-02 | 2013-01-03 | Idexx Laboratories, Inc. | Automated Calibration Method and System for a Diagnostic Analyzer |
| US9151769B2 (en) * | 2010-07-02 | 2015-10-06 | Idexx Laboratories, Inc. | Automated calibration method and system for a diagnostic analyzer |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1443317A (zh) | 2003-09-17 |
| RU2280270C2 (ru) | 2006-07-20 |
| WO2002006905A2 (fr) | 2002-01-24 |
| US20030158680A1 (en) | 2003-08-21 |
| JP2004510222A (ja) | 2004-04-02 |
| CA2418226C (fr) | 2011-09-20 |
| AU2001289682A1 (en) | 2002-01-30 |
| DE60106045D1 (de) | 2004-11-04 |
| EP1301832B1 (fr) | 2004-09-29 |
| WO2002006905A3 (fr) | 2002-05-16 |
| CA2418226A1 (fr) | 2002-01-24 |
| KR100810952B1 (ko) | 2008-03-10 |
| EP1301832A2 (fr) | 2003-04-16 |
| KR20030019593A (ko) | 2003-03-06 |
| DE60106045T2 (de) | 2006-02-09 |
| US7359830B2 (en) | 2008-04-15 |
| CN1193279C (zh) | 2005-03-16 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |