,the control system ,negative feedback versus positive feedback ,servo problem versus regulator problem ,development of block diagram ,measuring element ,controller and final control element
Instrumentation and process control fundamentalshossam hassanein
Basic course covers:
-Basic understanding of process control
-Important process control terminology
-Major components of a process loop
-Instrumentation P&ID symbols
Process Dynamics and Control (2007 Edition) (Hardbound)
By K. T. Jadhav
Size : B5, Pages: 428; Price : Rs. 390.00
Buy this book from : www.chinttanpublications.in
Introduction of process control, Process control, Example of controlled process, Feedback control system, Feed forward control system,Classification of variables in chemical process, Components of control system
Instrumentation and process control fundamentalshossam hassanein
Basic course covers:
-Basic understanding of process control
-Important process control terminology
-Major components of a process loop
-Instrumentation P&ID symbols
Process Dynamics and Control (2007 Edition) (Hardbound)
By K. T. Jadhav
Size : B5, Pages: 428; Price : Rs. 390.00
Buy this book from : www.chinttanpublications.in
Introduction of process control, Process control, Example of controlled process, Feedback control system, Feed forward control system,Classification of variables in chemical process, Components of control system
This presentation is made to provide the overall conceptual knowledge on Chilton Colburn Analogy. It includes basis, importance, assumption, advantages, limitations and applications in addition to the derivation. Make It Useful!
This Course basics of instrumentation and control systems used in oil and gas and petrochemical industry,
The course the following topics
Basics of Instrumentation
Field Instruments
Control Valves
Process Control
Control systems
In this presentation how flow rate, pressure, temperature and level in tank measure in refinery or any industry with different instrument are discussed.
This presentation is made to provide the overall conceptual knowledge on Chilton Colburn Analogy. It includes basis, importance, assumption, advantages, limitations and applications in addition to the derivation. Make It Useful!
This Course basics of instrumentation and control systems used in oil and gas and petrochemical industry,
The course the following topics
Basics of Instrumentation
Field Instruments
Control Valves
Process Control
Control systems
In this presentation how flow rate, pressure, temperature and level in tank measure in refinery or any industry with different instrument are discussed.
ommon motion systems use three types of control methods. They are position control, velocity control and torque control.
The majority of Newport’s motion systems use position control. This type of control moves the load from one known fixed position to another known fixed position. Feedback, or closed-loop positioning, is important for precise positioning.
Velocity control moves the load continuously for a certain time interval or moves the load from one place to another at a prescribed velocity. Newport’s systems use both encoder and tachometer feedback to regulate velocity.
Torque control measures the current applied to a motor with a known torque coefficient in order to develop a known constant torque. Newport’s motion systems do not employ this method of control.
it is a method of miscellaneous instrumental analytical technique. it is one of the thermal analytical techniques used. it also has wide applications in the field of pharmacy.
i hope, it will helpful to the students and peoples in the search of topics mentioned
it is informative to study to even get passing marks or for revision
This ppt describes some concepts in thermodynamics like entropy, change in entropy, change in entropy in reversible process, second law of thermodynamics, T-S diagram, Third law of thermodynamics, Heat death of universe, etc.
Types of Nuclear Reactors,BWR,Boiling Water Reactor,PWR,Pressurized Water Reactor,PHWR,Pressurised Heavy Water Reactor,GCR,Gas Cooled Reactor,AGR,Advanced Gas-Cooled Reactor,LGR-Light Water Cooled,Graphite Moderated Reactor,nuclear reactor
Current advancement in different gas liquid operationsSunny Chauhan
CURRENT ADVANCEMENT IN DIFFERENT GAS-LIQUID OPERATIONS,Gas Liquid operation equipment
,Extractive distillation
,Advances in Gas Absorption,High efficiency venturi scrubber
,Advances in Diffusion
,Advances in Stirred Tanks
,Advances in Distillation
,Advances in Venturi Scrubber
Excess gibbs free energy models,MARGULES EQUATION
,REDLICH-KISTER EQUATION,VAN LAAR EQUATION
,WILSON AND “NRTL” EQUATION
,UNIversal QUAsi Chemical equation
Management,administration and some basic principleSunny Chauhan
Management,administration and some basic principle,Defination of Management ,Management as art,Management as science,Scope of Management,Defination of Administration,Management and Administration ,Levels of Management
,Henri Fayol’s 14 Principles Of Management
Absorption & indusrial absorber,Gas Absorption,Equipments,Absorption in chemical Reaction,Absorption in Packed Tower,Absorption for counter current,Choice of Solvent,Continuous Contact Equipment,Height Equivalent to Theoretical Plate,HETP
The role of government in a disaster managementSunny Chauhan
What is Disaster?,What is disaster management ?,Components of Disaster Management, Principles of Disaster Management,Role of Government,CAPABILITIES & STRENGTH OF NDRF,ROLE OF NDRF,
Air pollution & Water pollution control lawsSunny Chauhan
Air pollution & Water pollution control laws,What is Air Pollution?,Control acts. For Air Pollution: ,FUNCTIONS OF BOARDS,PREVENTION AND CONTROL OF AIR POLLUTION,Water Pollution,Features of Act Water Pollution,Central Pollution Control Board’s Objectives,State Pollution Control Board’s Objectives
Equilibrium and types of equilibrium,Physical Equilibrium ,Chemical Equilibrium ,Law of Mass Action,The Equilibrium Constant (K),Relationship between Kc and Kp
Partial gibbs free energy and gibbs duhem equationSunny Chauhan
Partial gibbs free energy and gibbs duhem equation,relation between binary solution,relation between partiaL properties,PARTIAL PROPERTIES,PARTIAL PROPERTIES IN BINARY SOLUTION,RELATIONS AMONG PARTIAL PROPERTIES,Maxwell relation,Examples
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Hybrid optimization of pumped hydro system and solar- Engr. Abdul-Azeez.pdffxintegritypublishin
Advancements in technology unveil a myriad of electrical and electronic breakthroughs geared towards efficiently harnessing limited resources to meet human energy demands. The optimization of hybrid solar PV panels and pumped hydro energy supply systems plays a pivotal role in utilizing natural resources effectively. This initiative not only benefits humanity but also fosters environmental sustainability. The study investigated the design optimization of these hybrid systems, focusing on understanding solar radiation patterns, identifying geographical influences on solar radiation, formulating a mathematical model for system optimization, and determining the optimal configuration of PV panels and pumped hydro storage. Through a comparative analysis approach and eight weeks of data collection, the study addressed key research questions related to solar radiation patterns and optimal system design. The findings highlighted regions with heightened solar radiation levels, showcasing substantial potential for power generation and emphasizing the system's efficiency. Optimizing system design significantly boosted power generation, promoted renewable energy utilization, and enhanced energy storage capacity. The study underscored the benefits of optimizing hybrid solar PV panels and pumped hydro energy supply systems for sustainable energy usage. Optimizing the design of solar PV panels and pumped hydro energy supply systems as examined across diverse climatic conditions in a developing country, not only enhances power generation but also improves the integration of renewable energy sources and boosts energy storage capacities, particularly beneficial for less economically prosperous regions. Additionally, the study provides valuable insights for advancing energy research in economically viable areas. Recommendations included conducting site-specific assessments, utilizing advanced modeling tools, implementing regular maintenance protocols, and enhancing communication among system components.
Overview of the fundamental roles in Hydropower generation and the components involved in wider Electrical Engineering.
This paper presents the design and construction of hydroelectric dams from the hydrologist’s survey of the valley before construction, all aspects and involved disciplines, fluid dynamics, structural engineering, generation and mains frequency regulation to the very transmission of power through the network in the United Kingdom.
Author: Robbie Edward Sayers
Collaborators and co editors: Charlie Sims and Connor Healey.
(C) 2024 Robbie E. Sayers
Industrial Training at Shahjalal Fertilizer Company Limited (SFCL)MdTanvirMahtab2
This presentation is about the working procedure of Shahjalal Fertilizer Company Limited (SFCL). A Govt. owned Company of Bangladesh Chemical Industries Corporation under Ministry of Industries.
2. A control system is a device, or set of devices, that
manages, commands, directs or regulates the behavior
of other devices or systems.
Industrial control systems are used in industrial
production for controlling equipment or machines.
• There are two common classes of control systems :-
• open loop control system.
• closed loop control systems.
3. A liquid stream at a temperature Ti enters an insulated, well-stirred tank at a
constant flow rate w (mass/time). It is desired to maintain (or control) the
temperature in the tank at T R by means of the controller.
If the measured tank temperature T m differs from the desired temperature T R,
the controller senses the difference or error ε = T R-T m and changes the heat
input in such a way as to reduce the magnitude of e. If the controller changes
the heat input to the tank by an amount that is proportional to e , we have
proportional control.
4. COMPONENTS OF THE CONTROL SYSTEM:
1) Process (stirred-tank heater).
2) Measuring element (thermometer).
3) Controller
4) Final control element (variable transformer or control
valve).
5. The set point is a synonym for the desired value of the
controlled variable.
The load refers to a change in any variable that may cause
the controlled variable of the process to change.
6. The control system shown in Figure is called a closed-loop
system or a feedback system because the measured value of
the controlled variable is returned or “fed back” to a device
called the comparator.
In the comparator, the controlled variable is compared with
the desired value or set point.
If there is any difference between the measured variable and
the set point, an error is generated.
This error enters a controller, which in turn adjusts the final
control element to return the controlled variable to the set
point.
7. The feedback principle, which involves the use of the controlled variable
T to maintain itself at a desired value T R .
Negative feedback ensures that the difference between T R and T m is
used to adjust the control element so that the tendency is to reduce the
error.
For example : assume that the system is at steady state and that T T m T
R . If the load T i should increase, T and T m would start to increase,
which would cause the error e to become negative.
With proportional control, the decrease in error would cause the
controller and final control element to decrease the flow of heat to the
system, with the result that the flow of heat would eventually be reduced
to a value such that T approaches T R .
8. If the signal to the comparator were obtained by adding T R
and T m , we would have a positive feedback system.
assume that the system is at steady state and that Tm T R .
If Ti were to increase, T and T m would increase, which
would cause the signal from the comparator to increase,
with the result that the heat to the system would increase.
9. In the first situation, which is called the servomechanism-type (or
servo) problem, we assume that there is no change in load Ti and
that we are interested in changing the bath temperature according
to some prescribed function of time.
For this problem, the set point T R would be changed in accordance
with the desired variation in bath temperature.
If the variation is sufficiently slow, the bath temperature may be
expected to follow the variation in T R very closely.
EXAMPLES : The tracking of missiles and aircraft and the
automatic machining of intricate parts from a master pattern
10. The other situation will be referred to as THE
REGULATOR PROBLEM.
In this case, the desired value T R is to remain fixed,
and the purpose of the control system is to maintain
the controlled variable at T R in spite of changes in load
Ti.
This problem is very common in the chemical
industry.
11. Consider first the block for the process.
An unsteady-state energy balance around the tank
gives,
Where T0 is the reference temperature
At steady state, dT/dt is zero, and Above Eq. can be written
where the subscript s has been used to indicate
steady state.
12. Subtracting above equations gives,
If we introduce the deviation variables,
Ti
’ = Ti – Tis
Q = q – qs
T’ = T – Ts
so,
Now, Taking the Laplace transform
14. The temperature measuring element, which senses the bath
temperature T and transmits a signal T m to the controller, may
exhibit some dynamic lag.
In this example, we will assume that the temperature measuring
element is a first-order system, for which the transfer function is
MEASURING ELEMENT TRANSFER FUNCTION
where the input-output variables T’ and T’m are deviation variables,
defined as
T’ = T – Ts
Tm
’ = Tm - Tms
15. Note that when the control system is at steady state, Tms = Ts , which
means that the temperature measuring element reads the true bath
temperature.
The transfer function for the measuring element may be represented
by the block diagram shown in Above Fig.
16. It is assumed that the controller is a proportional controller.
The relationship for a proportional controller is
Where
TR = set- point temperature
Kc= Proportional sensitivity or
controller gain
A= Heat input when e =0
17. At steady state, it is assumed that the set point, the process temperature,
and the measured temperature are all equal to one another; thus
TRs = Ts - Tms
Let e’ be the deviation variable for error; thus
e' = e - es
where es = TRs - Tms.
Since TRs = Tms, es = 0
e' = e - 0 = e
This result shows that e is itself a deviation variable.
Since at steady state there is no error, and A is the heat input for zero
error,
18. So a proportional controller equation an be written as
Or
Where, Q = q-qs
The transform of above function gives
Note that e , which is also equal to e’ , may be expressed as
19. Process System Analysis & Control - Coughanower and Kappel, Mc-Graw
Hill Book Company.
https://en.wikipedia.org/wiki/Control_system
web.iku.edu.tr/courses/ee/ee670/ee670/lecture%20notes/ch01.pdf