MX9709813A - Metodo de regulacion de procedimientos de sintesis de productos quimicos. - Google Patents
Metodo de regulacion de procedimientos de sintesis de productos quimicos.Info
- Publication number
- MX9709813A MX9709813A MX9709813A MX9709813A MX9709813A MX 9709813 A MX9709813 A MX 9709813A MX 9709813 A MX9709813 A MX 9709813A MX 9709813 A MX9709813 A MX 9709813A MX 9709813 A MX9709813 A MX 9709813A
- Authority
- MX
- Mexico
- Prior art keywords
- tau
- variables
- reactor
- set values
- controlled
- Prior art date
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
- 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
- G05B13/04—Adaptive control systems, i.e. systems automatically adjusting themselves to have a performance which is optimum according to some preassigned criterion electric involving the use of models or simulators
- G05B13/048—Adaptive control systems, i.e. systems automatically adjusting themselves to have a performance which is optimum according to some preassigned criterion electric involving the use of models or simulators using a predictor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2/00—Processes of polymerisation
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F210/16—Copolymers of ethene with alpha-alkenes, e.g. EP rubbers
-
- 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
- G05B11/00—Automatic controllers
- G05B11/01—Automatic controllers electric
- G05B11/32—Automatic controllers electric with inputs from more than one sensing element; with outputs to more than one correcting element
-
- 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
- G05D—SYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
- G05D21/00—Control of chemical or physico-chemical variables, e.g. pH value
- G05D21/02—Control of chemical or physico-chemical variables, e.g. pH value characterised by the use of electric means
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2400/00—Characteristics for processes of polymerization
- C08F2400/02—Control or adjustment of polymerization parameters
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/582—Recycling of unreacted starting or intermediate materials
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Automation & Control Theory (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Artificial Intelligence (AREA)
- Computer Vision & Pattern Recognition (AREA)
- Evolutionary Computation (AREA)
- Medical Informatics (AREA)
- Software Systems (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Feedback Control In General (AREA)
- Polymerisation Methods In General (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Control Of Non-Electrical Variables (AREA)
Abstract
Un método de regulacion de un procedimiento de síntesis de al menos un producto químico en una instalacion que comprende al menos un reactor (R) que puede ser asimilado a un reactor perfectamente mezclado, en el que magnitudes de mando (GC) permiten actuar sobre el desarrollo del procedimiento de modo que una o varias magnitudes asociadas a las propiedades del producto y/o al desarrollo del procedimiento, denominadas magnitudes reguladas (GR), sean iguales a las consignas correspondientes (CGR), comprendiendo dicho método las etapas siguientes: (a) entrada de consignas concernientes a las magnitudes reguladas (CGR); (b) cálculo, por medio de un organo de prediccion (OP), de predicciones de las magnitudes reguladas (PGR), sobre la base de medidas de las magnitudes de mando del procedimiento (MGC), (c) utilizacion de un organo de control (OG) para calcular consignas de las magnitudes de mando del procedimiento (CGG), sobre la base de las consignas (CGR) y de las predicciones (PGR) de las magnitudes reguladas; (d) transmision de las consignas de magnitudes de mando del procedimiento (CGG) a accionadores con el fin de actuar sobre el desarrollo del procedimiento, en el que el organo de prediccion (OP) está basado en un modelo matemático del procedimiento, llamado modelo directo (M), y esta ideado de tal modo que se predice la masa MXR de al menos un constituyente (X) en el reactor (R) mediante la ecuacion: MXR=LAG(F. tx, tx), en la F es el caudal masivo del constituyente X que entra en el reactor R; t es el tiempo de permanencia de x en el reactor, la funcion y=LAG (u,t) es la solucion de la ecuacion diferencial t. dy/dt+y, calculada con el valor instantáneo de u y de t, así como con el ultimo valor de y calculado.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BE9500506A BE1009406A3 (fr) | 1995-06-09 | 1995-06-09 | Methode de regulation de procedes de synthese de produits chimiques. |
BE9500506 | 1995-06-09 | ||
PCT/EP1996/002408 WO1996041822A1 (fr) | 1995-06-09 | 1996-06-01 | Methode de regulation de procedes de synthese de produits chimiques |
Publications (2)
Publication Number | Publication Date |
---|---|
MX9709813A true MX9709813A (es) | 1998-03-31 |
MXPA97009813A MXPA97009813A (es) | 1998-10-15 |
Family
ID=
Also Published As
Publication number | Publication date |
---|---|
NO975780L (no) | 1998-02-06 |
HUP9803021A3 (en) | 1999-05-28 |
AU704563B2 (en) | 1999-04-29 |
NO315563B1 (no) | 2003-09-22 |
NO975780D0 (no) | 1997-12-08 |
CZ398597A3 (cs) | 1998-03-18 |
CA2220316A1 (fr) | 1996-12-27 |
HUP9803021A2 (hu) | 1999-04-28 |
JP2000500060A (ja) | 2000-01-11 |
CA2220316C (fr) | 2008-11-18 |
EP0830394B1 (fr) | 1999-03-17 |
PL186591B1 (pl) | 2004-01-30 |
WO1996041822A1 (fr) | 1996-12-27 |
DE69601794T2 (de) | 1999-10-07 |
BE1009406A3 (fr) | 1997-03-04 |
EP0830394A1 (fr) | 1998-03-25 |
CN1155626C (zh) | 2004-06-30 |
DE69601794D1 (de) | 1999-04-22 |
AU6124696A (en) | 1997-01-09 |
BR9609240A (pt) | 1999-05-11 |
EA000343B1 (ru) | 1999-04-29 |
RO120973B1 (ro) | 2006-10-30 |
PL323911A1 (en) | 1998-04-27 |
CN1192222A (zh) | 1998-09-02 |
EA199800049A1 (ru) | 1998-08-27 |
KR19990022784A (ko) | 1999-03-25 |
US6144897A (en) | 2000-11-07 |
UA37277C2 (uk) | 2001-05-15 |
ATE177761T1 (de) | 1999-04-15 |
CZ293002B6 (cs) | 2004-01-14 |
ES2131945T3 (es) | 1999-08-01 |
KR100432252B1 (ko) | 2004-09-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
HUP9803021A2 (hu) | Szabályozási eljárás és szabályozó kémiai termékek szintéziséhez | |
Kravaris et al. | Nonlinear controllers for trajectory tracking in batch processes | |
AU4079901A (en) | Process control system | |
ATE199188T1 (de) | System zur echtzeit optimierung und darstellung des gewinns | |
PL323049A1 (en) | Method of providing feedback signals in controlling non-linear processes | |
DK1069942T3 (da) | Parallel reaktor med intern registrering og metode til anvendelse af samme | |
CA2315637A1 (en) | Method of predicting overshoot in a control system response | |
GB2327627B (en) | Method of controlling the pressure in a simulated moving bed separation system | |
WO2000064650A8 (en) | Open-loop method and apparatus for producing a controlled blend of polyol and blowing agent | |
Asteasuain et al. | Industrial high pressure ethylene polymerization initiated by peroxide mixtures: A reduced mathematical model for parameter adjustment | |
Hinsberger et al. | Optimal temperature control of semibatch polymerization reactors | |
Guerra et al. | An activated-sludge-process application of integrated design and predictive control with instantaneous linearization | |
US4586126A (en) | Feed rate control | |
Nyttle et al. | Fuzzy logic control of a fed-batch fermentor with significant measurement delay | |
Calderon et al. | Waste analysis and minimization in batch and semibatch reactor operation through dynamic simulation and neural networks | |
Zhao et al. | A comparison of various control schemes for continuous bioreactor | |
EP0294052A2 (en) | Autoacceleration control for exothermic reactors | |
Samdani | Fuzzy logic: more than a play on words | |
Serac et al. | Design of a complex rule-based controller for a biotechnological process | |
Krallis et al. | Dynamic optimization of molecular weight distribution using orthogonal collocation on finite elements and fixed pivot methods: An experimental and theoretical investigation | |
Popescu et al. | Control and Optimization for Steel Plant Preheating Installations | |
Nortcliffe et al. | A variable transformation approach to in-line pH control | |
Schirrmeister et al. | MORPHYLANE- extraktivdestillation | |
Petrescu et al. | CONTROL AND OPTIMIZATION FOR COMPLEX STEEL PLANT HEATING INSTALLATIONS | |
Funke | Modellierung der Gewässerqualität mit Hilfe Markowscher Diffusionsprozesse |