WO2004012017A2 - Terme de transfert sans bosse (bumpless) pour systeme de controle - Google Patents
Terme de transfert sans bosse (bumpless) pour systeme de controle Download PDFInfo
- Publication number
- WO2004012017A2 WO2004012017A2 PCT/SG2002/000161 SG0200161W WO2004012017A2 WO 2004012017 A2 WO2004012017 A2 WO 2004012017A2 SG 0200161 W SG0200161 W SG 0200161W WO 2004012017 A2 WO2004012017 A2 WO 2004012017A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- term
- control
- bump
- transfer
- controller
- 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.)
- Ceased
Links
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
- G05B7/00—Arrangements for obtaining smooth engagement or disengagement of automatic control
- G05B7/02—Arrangements for obtaining smooth engagement or disengagement of automatic control electric
Definitions
- an error signal is derived in response to a measurement of a parameter it is desired to control.
- An automatic control signal is then derived from the error signal by a controller and used to control some aspect of the system to compensate the error.
- this control signal is made to be proportional to the error signal.
- components of the control signal are also produced which are the first order derivative or integral of the error signal. Controllers which employ these components are usually called proportional plus derivative (P+D) or proportional plus integral (P+I) controllers. It is also possible to have a so-called three term controller, i.e. proportional plus integral plus derivative (P+I+D or PID) controller.
- the derivative component is used if it is desired to reduce the lag (increase the response time of the system). Integral control is used primarily to eliminate offset, i.e. failure of the controlled parameter to return to exactly the required level (set point).
- the additional term 'BT(t)' in the control equation has a magnitude as well as what may be called as the bleed rate. This bleed rate is given in minutes or in seconds, and it should be set, like integral and derivative action rates by the process control engineer.
- the initial value of BT(t)' depends on the manual value of the output before the bump- less transfer to automatic control. Hence, the magnitude of 'BT(t)' is internally set, and is not externally set as its bleed rate.
- P+D controllers are rarely used, as whenever derivative action is used the integral term is invariably used. Further, the transfer from manual to automatic control is usually done in the steady state. Hence, there will be no difference in the error at the nth sampling interval and the (n-l)th sampling interval, and so the derivative action term will be zero. If this is not so, it is still advisable to neglect the term as it is small, and at this stage it can be quite unreliable. However, if it is not ignored, the initial value of 'BTn for a direct acting controller is as follows:
- Figure 1 shows five graphs.
- Graph A shows the level input versus the controller output for a direct acting controller with a gain of 1 and a bias value of 50%.
- Graph B shows a reverse acting controller with a gain of 1 and a bias value of 50%.
- Graph C shows a direct acting controller with a gain of 1 but with a bias value of 75%. From graph C it can be easily seen why when the bias value of a controller is set at other than the mid range value of 50%, it will result in a lopsided control system that is quite unacceptable.
- Graph D shows another lopsided control system if the bias value was set at 25%, when the level was at 50%.
- graph E shows a proportional control with a gain of 2, and a bias of 50%.
- a controller with a gain of 2 is also known as having a 50% proportional band (PB), while a gain of 1 is known as 100% PB.
- PB 50% proportional band
- FIG. 2 shows a level control system at the time of transfer from manual to automatic control.
- Figure 3 shows the same system when the value of BT(t) is zero, by which time the level in the tank has risen to 75%, assuming the flow into the tank has remained the same.
- the system consists of a tank (1) containing a liquid (2). It is filled from an uncontrolled liquid conduit (3), and it is desired to maintain the liquid between 0% and 100%.
- a displacer type of level sensing element (4), a level transmitter (5), and a DCS controller (6) are connected to a current to pneumatic positioner of a control valve (7).
- the controller in this case, is made to be a direct acting proportional only controller with a gain of 1 and a set-point of 50%.
- Such a controller will ensure that the system is controlled between the prescribed limits, in this case between 0% and 100%.
- the control valve chosen is such that it opens more as the controller output OP(t)' increases.
- the level in the tank was 50%, matching the set-point, and the manual output was 75%, for a bump-less transfer to take place the output of the controller has also to be 75%.
Landscapes
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- Automation & Control Theory (AREA)
- Feedback Control In General (AREA)
Abstract
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU2002320005A AU2002320005A1 (en) | 2002-07-08 | 2002-07-17 | Novel bump-less transfer term for control. system |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SG200204078-0 | 2002-07-08 | ||
| SG200204078 | 2002-07-08 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| WO2004012017A2 true WO2004012017A2 (fr) | 2004-02-05 |
| WO2004012017A3 WO2004012017A3 (fr) | 2006-04-20 |
Family
ID=31185901
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/SG2002/000161 Ceased WO2004012017A2 (fr) | 2002-07-08 | 2002-07-17 | Terme de transfert sans bosse (bumpless) pour systeme de controle |
Country Status (2)
| Country | Link |
|---|---|
| AU (1) | AU2002320005A1 (fr) |
| WO (1) | WO2004012017A2 (fr) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2470906A (en) * | 2009-06-08 | 2010-12-15 | Ove Arup & Partners Internat Ltd | Rainwater harvesting system |
| US9651923B2 (en) * | 2014-06-27 | 2017-05-16 | Manuel Jesubatham Pakianathan | Bump-less transfer term for proportional action controllers that eschew the integral action term |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4035620A (en) * | 1975-08-25 | 1977-07-12 | Phillips Petroleum Company | Bumpless control transfer |
| US5867384A (en) * | 1997-07-08 | 1999-02-02 | Johnson Services Company | Feedback controller |
-
2002
- 2002-07-17 WO PCT/SG2002/000161 patent/WO2004012017A2/fr not_active Ceased
- 2002-07-17 AU AU2002320005A patent/AU2002320005A1/en not_active Abandoned
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2470906A (en) * | 2009-06-08 | 2010-12-15 | Ove Arup & Partners Internat Ltd | Rainwater harvesting system |
| GB2470906B (en) * | 2009-06-08 | 2014-04-16 | Ove Arup & Partners Internat Ltd | Rainwater harvesting system |
| US9651923B2 (en) * | 2014-06-27 | 2017-05-16 | Manuel Jesubatham Pakianathan | Bump-less transfer term for proportional action controllers that eschew the integral action term |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2004012017A3 (fr) | 2006-04-20 |
| AU2002320005A1 (en) | 2004-02-16 |
| AU2002320005A8 (en) | 2004-02-16 |
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