1. The document describes several experiments related to process control systems, including temperature control loops, pressure control loops, flow control loops, and level control loops. It also covers programming a PLC and using a distributed control system.
2. The experiments are intended to study the elements of different control loops, take readings by varying set points, and observe the behavior of processes under control.
3. Programming concepts covered include logic gates, adders, multiplexers, and programming a PLC using ladder logic. The document also provides an overview of DCS systems and architectures.
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
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
Pneumatic control valve
Actual Pneumatic Control Valve
Typical Actuator & Valve
introduction to actuator
Actuator power
Actuator Fluids
Diaphragm Actuator
Positioner Indicator
Valve Body
Valve Plugs
Reverse & Direct Actuators
Air-To-Open vs. Air-To-Close
control valve
Controller Tuning
Selection of controller modes
Tuning Rules
Ziegler – Nichols Controller Settings
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
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
Pneumatic control valve
Actual Pneumatic Control Valve
Typical Actuator & Valve
introduction to actuator
Actuator power
Actuator Fluids
Diaphragm Actuator
Positioner Indicator
Valve Body
Valve Plugs
Reverse & Direct Actuators
Air-To-Open vs. Air-To-Close
control valve
Controller Tuning
Selection of controller modes
Tuning Rules
Ziegler – Nichols Controller Settings
,the control system ,negative feedback versus positive feedback ,servo problem versus regulator problem ,development of block diagram ,measuring element ,controller and final control element
Types of Controllers
Process control_ mechatronics engineering.
Control system is a combination of various elements connected as a unit to direct or regulate itself or any other system in order to provide a specific output is known as a Control system.
Components of a Control System
1.Controlled process: The part of the system which requires controlling is known as a controlled process.
2. Controller: The internal or external element of the system that controls the process is known as the controller.
3. Input: For every system to provide a specific result, some excitation signal must be provided. This signal is usually given through an external source. So, the externally provided signal for the desired operation is known as input.
TYPES OF DISTURBANCE:
1.an internal disturbance is generated within the system. 2.an external disturbance is generated outside the system and is an input.
Types of Control System:
1.Open loop control systems in this control system the
output is neither measured nor fed back for comparison
with the input.
2.Closed loop control systems in this control system the
actuating error signal, which is the difference between
the input signal and the feedback signal, is fed to the
controller so as to reduce the error and bring the output
of the system to a desired value.
PID
The PID control scheme is named after its three correcting terms, whose constitutes the manipulated variable (MV). The proportional, integral, and derivative terms are summed to calculate the output of the PID controller.
contents:
Ziegler-Nichols Closed-loop method.
Instrument Symbols.
continuous-mode controllers.
Proportional controller.
Derivative controller and another.
created by :Anaseem Alhanni.
University :Al- Balqa' Applied University (BAU).
In this presentation how flow rate, pressure, temperature and level in tank measure in refinery or any industry with different instrument are discussed.
,the control system ,negative feedback versus positive feedback ,servo problem versus regulator problem ,development of block diagram ,measuring element ,controller and final control element
Types of Controllers
Process control_ mechatronics engineering.
Control system is a combination of various elements connected as a unit to direct or regulate itself or any other system in order to provide a specific output is known as a Control system.
Components of a Control System
1.Controlled process: The part of the system which requires controlling is known as a controlled process.
2. Controller: The internal or external element of the system that controls the process is known as the controller.
3. Input: For every system to provide a specific result, some excitation signal must be provided. This signal is usually given through an external source. So, the externally provided signal for the desired operation is known as input.
TYPES OF DISTURBANCE:
1.an internal disturbance is generated within the system. 2.an external disturbance is generated outside the system and is an input.
Types of Control System:
1.Open loop control systems in this control system the
output is neither measured nor fed back for comparison
with the input.
2.Closed loop control systems in this control system the
actuating error signal, which is the difference between
the input signal and the feedback signal, is fed to the
controller so as to reduce the error and bring the output
of the system to a desired value.
PID
The PID control scheme is named after its three correcting terms, whose constitutes the manipulated variable (MV). The proportional, integral, and derivative terms are summed to calculate the output of the PID controller.
contents:
Ziegler-Nichols Closed-loop method.
Instrument Symbols.
continuous-mode controllers.
Proportional controller.
Derivative controller and another.
created by :Anaseem Alhanni.
University :Al- Balqa' Applied University (BAU).
In this presentation how flow rate, pressure, temperature and level in tank measure in refinery or any industry with different instrument are discussed.
Trabajo práctico tópicos de matemáticas (575)Carlos Rivera
Trabajo Práctico de la materia Tópicos de Matemáticas (575) de la carrera Educación mención Matemática de la Universidad Nacional Abierta (U.N.A.).
República Bolivariana de Venezuela
Soft skills training institute in ChandigarhPrem Thakur
The combination of people's skill which includes social skills, communication skills, characters features, career attributes and attitudes are called soft skills.
The Proto-Burst Buffer: Experience with the flash-based file system on SDSC's...Glenn K. Lockwood
Comparing the burst buffers of today, such as the Cray DataWarp-based burst buffer implemented on NERSC Cori, to the proto-burst buffer deployed on SDSC's Gordon supercomputer in 2012.
International Journal of Engineering Research and DevelopmentIJERD Editor
Electrical, Electronics and Computer Engineering,
Information Engineering and Technology,
Mechanical, Industrial and Manufacturing Engineering,
Automation and Mechatronics Engineering,
Material and Chemical Engineering,
Civil and Architecture Engineering,
Biotechnology and Bio Engineering,
Environmental Engineering,
Petroleum and Mining Engineering,
Marine and Agriculture engineering,
Aerospace Engineering.
Soft Computing Technique and Conventional Controller for Conical Tank Level C...ijeei-iaes
In many process industries the control of liquid level is mandatory. But the control of nonlinear process is difficult. Many process industries use conical tanks because of its non linear shape contributes better drainage for solid mixtures, slurries and viscous liquids. So, control of conical tank level is a challenging task due to its non-linearity and continually varying cross-section. This is due to relationship between controlled variable level and manipulated variable flow rate, which has a square root relationship. The main objective is to execute the suitable controller for conical tank system to maintain the desired level. System identification of the non-linear process is done using black box modelling and found to be first order plus dead time (FOPDT) model. In this paper it is proposed to obtain the mathematical modelling of a conical tank system and to study the system using block diagram after that soft computing technique like fuzzy and conventional controller is also used for the comparison.
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.
Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...Dr.Costas Sachpazis
Terzaghi's soil bearing capacity theory, developed by Karl Terzaghi, is a fundamental principle in geotechnical engineering used to determine the bearing capacity of shallow foundations. This theory provides a method to calculate the ultimate bearing capacity of soil, which is the maximum load per unit area that the soil can support without undergoing shear failure. The Calculation HTML Code included.
Cosmetic shop management system project report.pdfKamal Acharya
Buying new cosmetic products is difficult. It can even be scary for those who have sensitive skin and are prone to skin trouble. The information needed to alleviate this problem is on the back of each product, but it's thought to interpret those ingredient lists unless you have a background in chemistry.
Instead of buying and hoping for the best, we can use data science to help us predict which products may be good fits for us. It includes various function programs to do the above mentioned tasks.
Data file handling has been effectively used in the program.
The automated cosmetic shop management system should deal with the automation of general workflow and administration process of the shop. The main processes of the system focus on customer's request where the system is able to search the most appropriate products and deliver it to the customers. It should help the employees to quickly identify the list of cosmetic product that have reached the minimum quantity and also keep a track of expired date for each cosmetic product. It should help the employees to find the rack number in which the product is placed.It is also Faster and more efficient way.
Explore the innovative world of trenchless pipe repair with our comprehensive guide, "The Benefits and Techniques of Trenchless Pipe Repair." This document delves into the modern methods of repairing underground pipes without the need for extensive excavation, highlighting the numerous advantages and the latest techniques used in the industry.
Learn about the cost savings, reduced environmental impact, and minimal disruption associated with trenchless technology. Discover detailed explanations of popular techniques such as pipe bursting, cured-in-place pipe (CIPP) lining, and directional drilling. Understand how these methods can be applied to various types of infrastructure, from residential plumbing to large-scale municipal systems.
Ideal for homeowners, contractors, engineers, and anyone interested in modern plumbing solutions, this guide provides valuable insights into why trenchless pipe repair is becoming the preferred choice for pipe rehabilitation. Stay informed about the latest advancements and best practices in the field.
About
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
• Remote control: Parallel or serial interface.
• Compatible with MAFI CCR system.
• Compatible with IDM8000 CCR.
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
• Easy in configuration using DIP switches.
Technical Specifications
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
Key Features
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
• Remote control: Parallel or serial interface
• Compatible with MAFI CCR system
• Copatiable with IDM8000 CCR
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
Application
• Remote control: Parallel or serial interface.
• Compatible with MAFI CCR system.
• Compatible with IDM8000 CCR.
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
• Easy in configuration using DIP switches.
1. EXPERIMEN
T NO.
01
TITLE:
Study of Flow, Level, Pressure, Temperature processes and construction of
the P&I diagrams in accordance with
ISA guidelines /standards
DATE OF
EXPERIMENT
OBJECTIVE: A) TO UNDERSTAND AND REALIZE DIFFERENT SYMBOLS
.
B) APPLICATION OF P & I SYMBOLS FLOW , LEVEL , PRESSURE, TEMPARETURE
CONTROL LOOP
THEORY: While desigining complex control systems the follwing types of diagrams will be required:
a. Functional Diagram
b. Detailed Schematic Diagram
c. Inter connection Diagram
d. ISA Piping and Instrumentation Diagrams (P & I)
A P & I Diagram should provide information about the following :
1. The variable being measured
2. Indicating , Recording or other services, like control and alarm functions
3. Auxilliary Features of the instrument / the controller
4. Type of connecting lines
5. Approximate location of the point of measurement and control
6. Type of instrumentation to be included in the control centre at the processing end
CONCLUTION:
1
2. EXPERIMENT
NO.
02
TITLE:
Study of a Temperature Control Loop having Furnace, suitable final control
element, Temperature transmitter, conventional PID controller/Control
System, and data logger/recorder
DATE OF
EXPERIMENT
Objective:
I) To take different readings of the process value by varying the set point
II) To study different elements of Tempareture Control loop
Theory: There is a Muffle Furnace. The design temperature range of the furnace is 0-1000 degree C. The temperature
is sensed by a K-type thermocouple. The mV output (PV) is fed to remotely located SMART Temperature transmitter.
The signal is linearized and converted to 4-20 mA DC. This 4-20 mA DC (PV) is fed to the microprocessor based
single Loop Programmer cum PID controller (Local panel) as well as to DCS panel. The RAMP and SOAK time-temp
profile is programmed in TIC as well as in DCS. The controller process the PV input w.r.t SP and giving the corrective
output signal 4-20mA DC which is fed to the Thyristor power Controller to control the input power as per the temp set
point generated from TIC as well as DCS. There is remote/Local switch available on the Local Panel by which Control
through TIC or DCS can be selected.
In this particular experiment which is basically an example of a single fetch system, the measuring end of the RTD is
connected to the Muffle Furnace and both the voltage generated and temp of the RTD is fed to the control loop and
we can easily see them through the display.
Apparatus Table:
SI no. Name of the apparatus Quantity Specification Maker’s name
Observation Table:
SET POINT PROCESS VALUE
CONCLUTION:
2
3. EXPERIMENT
NO.
03
TITLE:
Study of a Pressure Control Loop having Pressure source, Pressure
Transmitter, Pneumatic
control valve, and conventional PID controller/Control System
DATE OF
EXPERIMENT
OBJECTIVE:
I) To observe the Pressure Control characteristics
II) To study different elements of Pressure Control loop
THEORY:
The Water is flowing from Bottom Tank through 1 inch pipeline. The pressure of water is measured by online smart
pressure transmitter giving 4 – 20 mA DC output (PV) proportional to Pressure. This 4 -20 mA DC output is fed to the
Microprocessor based Single Loop PID Controller (Local Panel) as well as to DCS panel. The Controller/ DCS
compares the PV input and gives the corrective output signal which is fed to I/P Converter for driving Pneumatic
Control Valve (PCV). By the % opening of PCV the pressure varies. There is Remote/ Local switch available on the
Local Panel by which Control through PIC or DCS can be selected.
Apparatus Table:
SL NO. NAME SPECIFICATION MAKER’S NAME
PROCEDURE:
1) The process fluid is flowed in the pipeline using a pump.
2) The process fluid passes through two different pipes, one flows back to the tank via a valve.
3) The pressure transmitter provides an electrical I/P to the process value of the PID Controller. It also shows the % of
opening or closing of the valve.
4) The set point of the Controller can be given manually or through DCS.
5) The error signal generated due to the difference between PV and SP value is fed to the I/P Converter which
generates a pneumatic signal.
6) The pneumatic signal and the pneumatic supply of the air regulator is fed to the signal of the actuator.
7) The actuator controls the valve. Thus the flow of the fluid is also controlled and the pressure is also controlled.
3
4. OBSERVATION TABLE:
SL
NO.
SP PV SMART
PRESSURE
TRANSMITTE
R READING
STEM
LENGT
H (mm)
SETTLING
TIME (s)
POSITIONER
I/P SIGNAL
(Kg/ Cm2
)
O/P (Kg/
Cm2
)
CONCLUSION:
4
5. EXPERIMENT
NO.
04
TITLE:
Study of a Flow Control Loop having suitable Flow meter, Pneumatic
control valve, and conventional PID controller/Control System
DATE OF
EXPERIMENT
OBJECTIVE :
(I) To study the changing pattern of flow rate characteristics of process fluid
(II) To study different elements of Flow Control loop
THEORY: The water is flowing from the overhead Tank through 1 inch Pipe. The flow of water is measured by
Honeywell make Magnetic flow meter, it gives 4-20 mA DC output (PV) proportional to water flow rate (0-16 LPM).
This 4-20mA DC output is fed to the Honeywell make Microprocessor based Single Loop PID Controller (local panel)
as well as to DCS panel. The controller processes the PV input w.r.t SP and giving the corrective output signal, it is
fed to I/P Converter where 4-20 mA DC current signal has been converted to 0.2 to 1 Kg/cm2
and is fed to the
Pneumatic Control Valve located on the flow line to control the desired flow rate as per the Set Point generated from
SLC as well as Honeywell make DCS. There is Remote/Local switch available on the Local Panel by which Control
through SLC or DCS can be selected. We can include variable area flow meter (Rotameter) on the same to check the
flow rate.
Apparatus Table:
SL. No. NAME OF APPARATUS RANGE/SPECIFICATION MAKER’S NAME
5
6. PROCEDURE:
1) Process fluid is at first stored in the tank kept at ground level. Then the pump draws the process fluid from the
lower tank towards the pipelines and then via the pipelines it flows towards the tank kept at the higher level. The fluid
from the higher tanker flows back to the ground level tanker via a flow-transmitter and a Pneumatic Valve kept in
series.
2) The flow transmitter provides an electrical i/p to the process value field of the controller. The controller compares
this i/p value with the value that is provided in the Set Point field of the controller either through mode or through
DCS based system and thus generates an electrical o/p signal which can be called an Error signal.
3) This, fed into the I/P Converter, obtains the signal from the supply of Air Regulator and thus converts the o/p signal
into pneumatic signal which in turn is fed into the positioner.
4) Air Regulator also provides pneumatic supply to the positioner. The positioner compares the signals obtained from
I/P Converter and air regulator and generates an error o/p in the form of pneumatic signal and this is provided to the
actuator to control the valve action.
5) By valve action, water in the ground level tank will increase (or decrease). Difference in pressure between the two
tanks gives the flow rate a positive value.
OBSERVATION TABLE :
SL. No. CONTROLLER READING
PV SP
SMART TXO
READING (%)
ROTAMETER
READING
CONCLUSION :
6
7. EXPERIMENT
NO.
05
TITLE:
Study of a typical Level Control Loop having Level Transmitter,
Motorized control valve, and conventional PID controller/Control System
DATE OF
EXPERIMENT
Objective:
I) To Study the level characteristics when it is controlled by PID controller.
II) To study different elements of Level Control loop
Theory:
The water is flowing from the bottom tank through 1 inch pipe to top tank where level of water is maintained. The
water level is measured by Honeywell made Ultrasonic level transmitter giving 4- 20 amp DC output (PV)proportional
to water level .This 4- 20 amp DC output is fed to PID controller as well as to DCS panel. The controller processes the
PV input with respect to SP and giving the corrective output signal , which is fed to Honeywell made electrically
operated linear control valve located on the incoming flow line to control the desired level as per the set point
generated from PID as well as DCS.There is remote / local switch available on the local panel by which control
through PID or DCS can be selected.
Apparatus Table:
SI no. Name of the
apparatus
Quantity Specification Maker’s name
Procedure :
1. Power is supplied to the system.
7
8. 2. Local mode control is selected in the PID controller.
3. A set point is provided and the pump is turned on.
4. The electronic actuator is controlled by the PID controller to obtain the set point value .
5. The Process Variable (PV) value is shown on the display of PID controller. The ultrasonic level sensor sends
the signal which corresponds to the level of the tank in terms of current signal to the PID controller.
6. PID controller transforms it into PV value The valve actuator control depends on this PV value.
7. The maximum overshoot and undershoot PV value, and the position of valve stem and settling time is also
measured.
Observation Table :
SI no. Set Point(SP) Process
variable(PV)
Max.
overshoot
Max.
undershoot
Valve stem
length
Settling time
Conclusion :
8
9. EXPERIMENT
NO.
06
TITLE:
Study of a Air Duct Flow Monitoring and Control
DATE OF
EXPERIMENT
OBJECTIVE:
TO STUDY THE MONITORING OF AIR DUCT FLOW BY
I) POT CONTROL MODE
II) AUTO CONTROL MODE
THEORY :
There is a fan blower which is mechanically connected to a1 horse power 1400rpm 1 phase motor. Once
the motor gets powered the fan blower sucks the air from the atmosphere and delivers through a tunnel where the flow
of air is measured continuously by an orifice plate with the help of a flow transmitter. The DP across the orifice plate
is measured by flow transmitter giving 4- 20 m Amp DC output proportional to the square root of air flow rate. This 4
– 20 m amp Dc(PV)is fed to the PID controller. The controller processes the PV input with respect to SP and giving
the corrective output signal 0-10 V DC to a VFD drive and a electrical actuator mounted on the inlet of the
pipeline. There is a change over switch is available on the local panel by which control can be done by either
VFD /Electrical Actuator.
9
10. PROCEDURE:
(1) Power supplied to the system.
(2) POT control mode is selected.
(3) RPM of the pump is controlled from RPM controller.
(4) PV value is noted by changing SP.
(5) Auto control mode is selected.
(6) SP is set ,RPM of pump is auto adjusted.
APPARATUS TABLE:
SL NO. NAME OF THE APPARATUS SPECIFICATION QUANTITY
OBSERVATION TABLE:
FOR POT CONTROL:
SL NO. CONTROLLER
SP PV
DPT
O/P
REMARK
10
11. FOR AUTO CONTROL:
SL NO. CONTROLLER
READING
SP PV
DPT
O/P
REMARK
CONCLUSION:
EXPERIMENT
NO.
07
TITLE:
PLC Programming through PC
DATE OF
EXPERIMENT
Objective:
I)To study PLC and design the digital logic circuits using ladder logic programming
II) Design PLC based instrumentation experiments
Theory:
A programmable logic controller, PLC is a digital computer used for automation of typically industrial
electromechanical process such as control of machinery on factory usually lines etc. PLC’s are designed for multiple
arrangements of digital and analog inputs and outputs executed temperature ranges immunity to electrical noises and
resistance to vibration and impact. Programs to control machine operation are typically stored in battery backup or
non- volatile memory.
Most recently PLC are programmed using application software a personal computer. PC is connected to PLC through
RS-232 protocol. The programming software allows entry and editing of ladder logic.
11
12. PLC Module-Master Logic 50:
It is Honeywell’s ML50 compact PLC with high performance and functionality, which can be used as I/O and as a
stand Alone PLC or as a distributed control.
Features: The system has following high performances-
i) CPU processing speed (bit):160 ns/step.
ii) Max 480 I/O control supporting small and mid-sized system instrumentation.
iii) Max 10K steps of large program capacity.
iv) Expanded application with the support of floating print.
Soft master:
It is a software used for interfacing Honeywell ML50 PLC module to PC and the software also provides the platform
for PLC programming and uploading it to PLC module.
Communication-FAST ETHERNET:
Here fast Ethernet is used which is much more faster than RS-232 protocol. Features are-
• Model: MLL-EMTA.
• Communication spec: 10/100 Base-TK.
• Protocol: TCP/IP, UDP/IP.
• HS Link Sending/Recording: 200 words/Block.
• No. of channels connectable to upper stage: 8 channels.
Apparatus Table:
SI. no. Name of the apparatus Quantity Specification Maker’s Name
Procedure:
i) Turn on the PLC module.
ii) Program is written on software.
iii) Then connect it to PLC module and click on RUN.
12
13. iv) According to the program, i/p is given and corresponding o/p is observed.
Observation table:
Programs:
(1) NOT GATE:
Boolean Expression Q= NOT A or
Truth table:
Input(A) Output(Q)
(2) OR GATE:
Boolean Expression Q= A+B
Truth table:
Input(A) Input(B) Output(Q)
(3) AND GATE:
Boolean Expression Q= A.B
Truth table:
(4) NAND GATE:
Boolean Expression Q=
Truth table:
13
Input(A) Input(B) Output(Q)
Input(A) Input(B) Output(Q)
15. Truth tab
Input(A) Input(B) SUM (S) CARRY(C)
le:
(9) FULL ADDER CIRCUIT
Boolean Expression Q =
Truth table:
Input(A) Input(B) Input (C) SUM (S) CARRY(C)
10) HALF SUBTRACTOR CIRCUIT
Boolean Expression Q=
Truth table:
Input(A) Input(B) DIFFERENCE(D) BORROW(B)
11) FULL SUBTRACTOR CIRCUIT
Boolean Expression Q=
15
16. Truth table:
Input(A) Input(B) Input (C) DIFFERENCE
(D)
BORROW(B)
12) 4:1 MULTIPLEXER CIRCUIT
Boolean Expression Q=
Truth table:
Selection Line 1 Selection Line 2 Output(Q)
Conclusion:
EXPERIMENT
NO.
08
TITLE:
DCS based Instrumentation Experiments
DATE OF
EXPERIMENT
16
17. Objective:
I) Introduction to DCS system and its Architecture, Operation, Applications
II) To operate and study the behaviour of Pressure Control Loop , Flow Control Loop , Level Control Loop
and
Tempareture Control Loop in DCS mode
Theory:
A distributed control system (DCS) refers to a control system usually of a manufacturing system, process or any kind
of dynamic system, in which the controller elements are not central in location but are distributed throughout the
system with each component sub system controlled by networks for communication and monitoring .DCS is a very
broad term used in variety of industries, to monitor & control distributed components.
CENTUM is the generic name of distributed control system for small and medium scale plants (CENTUM CS1000),
and for large scale plants (CENTUM CS3000).
Block diagram:
17
18. (Diagram of the hardware architecture CENTUM CS 1000)
Architecture:
The CENTUM CS 1000 architecture can be subdivided into several units namely CPU, Battery units, I/O Modules,
communication cards, Human Interface System(HTS).
i)CPU : There are two models of CPU card. The CP701 for basic systems and CP703 for enhanced systems. CP701
model has 8MB memory but CP703 model has 16 MB memory. The model chosen depends on the type of system
software used. The main memory is ensured of the high reliability by error correction code(ECC).
ii)Power supply cord: The power supply cord is designed to supply power to the common nets such as the as CPU
cards, and up to five I/O modules nests. Standardizing the output voltages to +5v DC has simplified the circuit and
structure and reduced the no of parts.
iii)Input and Output modules: The I/O modules convert the analog or digital signals from the field equipment
then pass to field control stations or vice versa to convert the signals from field control stations for the field
equipments.
iv)Communication cards: The communication cards are used to realize the general purpose communication of
field control station and subsystems via serial links, so that the subsystem may be controlled or monitored .
18
19. v)Human Interface System(HTS): These are different operational and monitoring windows, which have to
define during designing the HTS. The human interface system programmed for a project or plan is designed in such a
way that it would be easy for the operator to understand all the operations occurring in the plant.
RS 232: RS 232 is a standard communication protocol for linking computer and its peripheral devices to allow serial
data exchange. In simple terms RS 232 defines the voltage for the path used for data exchange between the devices. It
specifies common voltage and signal level, common pin wire configuration and minimum, amount of control signals.
Hart Protocol: HART ("Highway Addressable Remote Transducer") is a communication protocol designed for
industrial process measurement and control applications. It's called a hybrid protocol because it combines analog and
digital communication. It can communicate a single variable using a 4-20 ma analog signal, while also communicating
added information on a digital signal. The digital information is carried by a low-level modulation superimposed on
the standard 4-to-20 mA current loop.
The digital signal does not affect the analog reading because it's removed from the analog signal by standard filtering
techniques.
The ability to carry this added digital information is the basis for HART's key benefits.
Advantage: Traditional analog and discrete devices communicate only a single process variable — and you typically
have no easy way to tell if the information they're sending is valid.
With HART, you still get the process variable — but other types of information, too. Examples include
• Device Status & Diagnostic Alerts
• Process Variables & Units
• Loop Current & % Range
• Basic Configuration Parameters
• Manufacturer & Device Tag
HART devices that are digitally polled by a host can tell you if they're correctly configured and operating correctly.
This eliminates the need for most routine checks — and helps you detect failure conditions before they cause a major
process problem.
Hart protocol specification:
The HART Protocol implements layers 1,2, 3, 4 and 7 of the Open System Interconnection (OSI) 7-layer protocol
model:
The HART Physical Layer is based on the Bell 202 standard, using frequency shift keying (FSK) to communicate at
1200 bps. The signal frequencies representing bit values of 0 and 1 are 2200 and 1200Hz respectively. This signal is
superimposed at a low level on the 4-to-20mA analog measurement signal without causing any interference with the
analog signal.
The HART Data Link Layer defines a master-slave protocol - in normal use, a field device only replies when it is
spoken to. There can be two masters, for example, a control system as a primary master and a handheld HART
communicator as a secodary master. Timing rules define when each master may initiate a communication transaction.
Up to 15 or more slave devices can be connected to a single multidrop cable pair.
The Network Layer provides routing, end-to-end security, and transport services. It manages "sessions" for end-to-
end communication with correspondent devices.
The Transport Layer: The Data-Link Layer ensures communications are successfully propagated from one device to
another. The Transport Layer can be used to ensure end-end communication is successful.
The Application Layer defines the commands, responses, data types and status reporting supported by the Protocol.
In the Application Layer, the public commands of the protocol are divided into four major groups:
1. Universal Commands - provide functions which must be implemented in all field devices
19
20. 2. Common Practice Commands - provide functions common to many, but not all field devices
3. Device Specific Commands - provide functions that are unique to a particular field device and are specified
by the device manufacturer
4. Device Family Commands - provide a set of standardized functions for instruments with particular
measurement types, allowing full generic access without using device-specific commands.
SCADA(Supervisory Control and Data Acquisition): SCADA (supervisory control and data acquisition) is a
category of software application program for process control, the gathering of data in real time from remote locations
in order to control equipment and conditions. SCADA is used in power plants as well as in oil and gas refining,
telecommunications, transportation, and water and waste control.
SCADA systems include hardware and software components. The hardware gathers and feeds data into a computer
that has SCADA software installed. The computer then processes this data and presents it in a timely manner. SCADA
also records and logs all events into a file stored on a hard disk or sends them to a printer. SCADA applications warn
when conditions become hazardous by sounding alarms.
SCADA diagram:
Application of DCS: Today’s controllers have extensive computational capabilities and in additional to proportional,
integral and derivative (PID) control, can generally perform logic and sequential control. Modern DCS also support
neural networks and fuzzy applications.
DCSs are dedicated systems used to control manufacturing processes that are continuous ar batch oriented such as:-
Electrical power grids and electrical generation plants.
Environmental control systems.
Traffic signals.
Radio signals.
Water management systems.
20
21. Oil refining plants.
Metallurgical process plants.
Chemical plants.
Pharmaceutical manufacturing.
Sensor networks.
Conclusion:
21