GB1255541A - Method for the automatic control of a process - Google Patents
Method for the automatic control of a processInfo
- Publication number
- GB1255541A GB1255541A GB1238169A GB1238169A GB1255541A GB 1255541 A GB1255541 A GB 1255541A GB 1238169 A GB1238169 A GB 1238169A GB 1238169 A GB1238169 A GB 1238169A GB 1255541 A GB1255541 A GB 1255541A
- Authority
- GB
- United Kingdom
- Prior art keywords
- variables
- alternative
- flow
- automatic control
- march
- 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.)
- Expired
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
- G05B15/00—Systems controlled by a computer
- G05B15/02—Systems controlled by a computer electric
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/42—Regulation; Control
- B01D3/4211—Regulation; Control of columns
- B01D3/4227—Head- and bottom stream
Landscapes
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Automation & Control Theory (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Control Of Non-Electrical Variables (AREA)
- Feedback Control In General (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
1,255,541. Automatic control systems. SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ N.V. March 10, 1969 [March 12, 1968], No.12381/69. Heading G3R. A method for the automatic control of a number of process variables by a digital computer in response to measured values of the variables is characterized by the provision of at least one alternative programme for use in the event of a disturbance in the operation of the process equipment or a part thereof. Change-over to the alternative programme may be automatic, and it may be designed to provide reduced normal product and/or a gradual termination of the process. The invention is described in relation to two alternative processes, a distillation system, Fig.1 (not shown) and a catalytic reforming process for hydrocarbons, Fig.2 (not shown). In the first of these pressure, fluid-flow and liquid level are measured at various points and if any of them are outside upper and lower limits the alternative programme is used to adjust e.g. the feed, condenser coolant flow, the flow in re-circulatory loops &c. until the variable is restored to within the limits. In certain cases a second and different correcting action is made if the first is insufficient. The system includes means for keeping the ratio between certain quantities constant so that corrective action is applied to both. The second system uses similar control arrangements of these same variables, and in addition the temperature in reactor vessels is kept constant by adjustment of heater fuel supply, and if the temperature drops below a minimum value the set point of a feed control system is lowered. The normal operation of these systems is not described in detail, and neither is the computer.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL6803525A NL6803525A (en) | 1968-03-12 | 1968-03-12 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1255541A true GB1255541A (en) | 1971-12-01 |
Family
ID=19803011
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1238169A Expired GB1255541A (en) | 1968-03-12 | 1969-03-10 | Method for the automatic control of a process |
Country Status (5)
Country | Link |
---|---|
CA (1) | CA950561A (en) |
DE (1) | DE1912061A1 (en) |
FR (1) | FR2003701A1 (en) |
GB (1) | GB1255541A (en) |
NL (1) | NL6803525A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4775949A (en) * | 1986-06-27 | 1988-10-04 | K-Tron International, Inc. | Weigh feeding system with stochastic control |
US4893262A (en) * | 1986-06-27 | 1990-01-09 | K-Tron International, Inc. | Weigh feeding system with self-tuning stochastic control |
US4954975A (en) * | 1988-08-10 | 1990-09-04 | K-Tron International, Inc. | Weigh feeding system with self-tuning stochastic control and weight and actuator measurements |
WO2012020154A1 (en) * | 2010-07-29 | 2012-02-16 | Universidad De Malaga | Monitoring and control system and method for a distillation column |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1404761A (en) * | 1970-05-26 | 1975-09-03 | Toyoda Automatic Loom Works | Method of controllig a spinning operation |
DE2360757C2 (en) * | 1973-12-06 | 1986-12-04 | Metallgesellschaft Ag, 6000 Frankfurt | Automatic control of a process for the thermal gasification of hydrocarbons with oxygen and water vapor |
FR3109104B1 (en) | 2020-04-14 | 2022-10-14 | Psa Automobiles Sa | Structural glue spray nozzle covered by a protective layer against the accumulation of structural glue residue |
-
1968
- 1968-03-12 NL NL6803525A patent/NL6803525A/xx unknown
-
1969
- 1969-03-10 DE DE19691912061 patent/DE1912061A1/en active Pending
- 1969-03-10 FR FR6906676A patent/FR2003701A1/fr not_active Withdrawn
- 1969-03-10 GB GB1238169A patent/GB1255541A/en not_active Expired
- 1969-03-10 CA CA045,226,A patent/CA950561A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4775949A (en) * | 1986-06-27 | 1988-10-04 | K-Tron International, Inc. | Weigh feeding system with stochastic control |
US4893262A (en) * | 1986-06-27 | 1990-01-09 | K-Tron International, Inc. | Weigh feeding system with self-tuning stochastic control |
US4954975A (en) * | 1988-08-10 | 1990-09-04 | K-Tron International, Inc. | Weigh feeding system with self-tuning stochastic control and weight and actuator measurements |
WO2012020154A1 (en) * | 2010-07-29 | 2012-02-16 | Universidad De Malaga | Monitoring and control system and method for a distillation column |
ES2374931A1 (en) * | 2010-07-29 | 2012-02-23 | Universidad De Málaga | Monitoring and control system and method for a distillation column |
Also Published As
Publication number | Publication date |
---|---|
FR2003701A1 (en) | 1969-11-14 |
DE1912061A1 (en) | 1969-10-02 |
NL6803525A (en) | 1969-09-16 |
CA950561A (en) | 1974-07-02 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2908734A (en) | Method of and apparatus for controlling catalytic processes | |
GB1255541A (en) | Method for the automatic control of a process | |
CA1170335A (en) | Nonlinear control of liquid level | |
ES8403632A1 (en) | Reactor temperature control systems and methods. | |
GB1420671A (en) | Automatic control system for optimizing performance of process units | |
GB1466429A (en) | Control apparatus for fractionation tower | |
US3174298A (en) | Process controller | |
US4617092A (en) | Process for controlling a distillation column | |
GB1097065A (en) | Improvements in or relating to heat transfer systems | |
SE8404776D0 (en) | SET TO REGULATE REDUCTION OF ZIRCONIUM | |
US3351430A (en) | Method for the automatic control of reactions in continuous flow reaction series | |
US3172880A (en) | Temperature control for chemical reaction vessels | |
ES402035A1 (en) | Pressure monitored temperature controlled system for a liquid-vapor process | |
US3408261A (en) | Control system for fractional distillation having a non-linear function generator | |
SU390137A1 (en) | METHOD OF AUTOMATIC CONTROL OF THE VARIABLE COLUMN BRAHRECTIFICATION APPARATUS | |
US2670278A (en) | Apparatus for controlling bed depth in conversion systems | |
GB1024316A (en) | Method of, and apparatus for, controlling a continuously operating distillation process | |
US3518060A (en) | Apparatus for converting uo3 to uf4 | |
GB1350132A (en) | Process and apparatus for controlling a distillation column | |
US3196189A (en) | Method of controlling a dehydrogenation process | |
GB1481539A (en) | Constraint control for processes with equipment limitations | |
GB1391276A (en) | Control system | |
US3558588A (en) | Exothermic process control | |
US3175764A (en) | Pneumatic compensating control circuit to minimize process dead time | |
UST934006I4 (en) | Oop flow |