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Final Report
GRADUATE ACT. APPRENTICESHIP TRAINING
(28Th OCTOBER 2014 – 28Th OCTOBER 2015)
S.ARUN
Employee No: 600317
B.E & Diploma – ELECTRONICS AND COMMUNICATION
ENGINNERING
SRF LIMITED – TECHNICALTEXTILESBUSINESS MANALI
ACKNOWLEDGEMENT
I am immensely grateful to Mr. V. Sekar (Senior Vice President-Operations &
complex heads office), SRF LIMITED TTB-Manali, Chennai, for providing the opportunity
to get trained and learn in this premier organization.
I am immensely thankful to Mr. Narayanan Athmanathan (Deputy General
Manager) for providing the opportunity and required facilities.
I am immensely thankful to Mr. KALAI SELVAN (Chief Manager) HR for
providing the opportunity and required facilities.
I express my gratitude and sincere thanks to Mr. VIVEK SINGH SENGAR- Chief
Manager (Instrumentation) for his co-operation, invaluable guidance and motivation.
I am indebted to [Mr.S.Arunarokiadass, Assistant Manager, Mr.Suvajit Roy, senior
Executive] of Instrumentation department, for his invaluable support and supervision
throughout the training period, which had kept this training on track.
In the course of training at SRF Limited- TTBM, I had learnt a lot about this
organization and also about the latest on goings and development in Instrumentation field. I
express my sincere thanks to all the members who have helped directly and indirectly.
Without their help and guidance I wouldn’t have been able to successfully complete my
training worth fully.
CERTIFICATE
This hereby certify that the work which is being presented for the award of
Apprentice Certificate, submitted at SRF Limited, Manali is an authentic record
of Mr.S.ARUN carried out under the supervision of Mr. VIVEK SINGH
SENGAR, Chief Manager of (Instrumentation).
This certification represents excellence in his learning skills also represents
his attitude, obedient and sincerely in his work and the way he towards involving
himself in mixing up with high standards and self-responsibilities and progress
through success and knowledge.
He also serviced electronics’ and instrument’s which are added in the list.
This is to certify that the above statement made by the candidate is correct
to the best of my knowledge.
(Mr. Vivek Singh Sengar)
Chief Manager - Instrumentation
SRF Limited-TTBM
Chennai – 600068.
SRF LIMITED
PROFILE:
The SRF is a multi-business entity engaged in the manufacturing of chemical based
industrial intermediates. Established in 1973, SRF has today grown into a global enterprise
with operations in 4 countries. With headquarters in Gurgaon, India, the $450 million company
has operations in three more countries, UAE, Thailand and South Africa. Apart from Technical
Textiles Business, in which it enjoys a global leadership position, SRF is a domestic leader in
Refrigerants, Engineering Plastics and Industrial Yarns as well. The company also enjoys a
significant presence among the key domestic manufacturers of Polyester Films and
Fluorospecialities.
Building on its in-house R&D facilities for Technical Textiles Business and Chemicals
Business, the company strives to stay ahead in business through innovations in operations and
product development.
A winner of the prestigious Deming Application Prize for its tyre cord business, SRF continues
to redefine its work and corporate culture with the TQM as its management way.
SRF Today - a snapshot
 Rs. 2000 crore multi-product, multi-business organizations.
 Market leader in Technical Textiles, Refrigerants, Engineering Plastics and Industrial
Yarns.
 Manufacturing plants spread over 8 locations in India, one in Dubai, one in South Africa
and one in Thailand.
 World's 2nd largest producer of Nylon 6 tyre cord fabrics.
 World's 2nd largest producer of belting fabrics.
 Exporting to over 60 countries.
Process Overview
Capro Lactam Chips Yarn Undipped Fabric
Molten Lactam Additives Ply Dipped Fabric
Polymer Polymer Cord Tyre Cord fabric
Chips Yarn Fabric
Polymerization
Dipping
Spinning
Twisting and Loom
NEW YARN PLANT - POLYMERIZATION:
The NYP Ploy plant is the first stage, where the raw material “caprolactam”
is fed, treated at confined conditions then made into polymer and pelletized into polymer chips
stored in the silos.
Instrumentation plays a vital role in this plant with high end technology, because the
plant uses most of the transmitters and control valves of “FOUNDATION Fieldbus”
technology; which is all digital, duplex, self-diagnostics and multidrop technology and
“Profibus” for drives with “DELTA V” DCS. Also it uses conventional on/off valves,
temperature sensing elements etc.
The temperature in the entire process should be maintained at the specified limits and
the product should not be oxidized, so as to maintain the quality of the final product. The entire
process involves mainly closed loops which are feedback type; also the process has multiple
interlocks for safe operation.
The entire plant is controlled by three DELTA V MD controllers (1, 2, 3) where
controller 1 is assigned to discrete instruments, controller 2 is assigned to analog instruments
and the controller is assigned to De-Polymerization area. The entire plant is operated by 2
Operator Work Stations (OWS), which is controlled by a Professional plus station (DVINST).
The process parameters such as pressure, level and DP flow where measured using the
Rosemount 3051(FF) type transmitters and Yokogawa D-Harp type etc. Mass flow is measured
using the multi parameter measuring Micro Motion F-series (FF) Coriolis sensors and 2700
Micro Motion transmitters. The magnetic flow meters are of Rosemount 8742C
(FF)Most of the control valves are of Samson 3730-5 (FF) make. The point level is measured
using vibrating fork and capacitance type level switches of Sapcon make, and uses temperature
sensors such as PT100, K type thermocouples and also other instruments such Trace Oxygen
analysers, Solenoid valves, Rotameter’ s etc.,.
NEW YARN PLANT - SPINNING:
The NYP Spinning is the second stage of the process, where the polymer
chips mixed with CUI then heated and melted at specified temperature and pressure then
quenched and made into fine filaments of yarn and rolled up in the bobbins. The plant is in
technical collaboration with TMT Machinery Co, Japan.
There are four chip receiving silos, the chips from the silos in poly are transferred to
the nine unit’s CRS1 through the Nitrogen pressure and it is incorporated with vibrating fork
level switches so as to indicate the level. Then the chips are mixed in 20(Chips):4(CUI) ratio
in the ASM area which is controlled by a Siemens S7 PLC, the inputs and outputs are connected
to the DCS through the Remote I/O sub-system 1. The load in the hoppers are measured by
load cells A-stuff (S type), B-stuff (Single Ended) then mixed and fed to CRS 2.the CRS 2 &
3 are maintained at below atmospheric pressure. Also these silos have pressure switches,
gauges, vibrating fork level switches and solenoid valves etc. which are connected to the DCS
through the Remote I/O sub-system 2 and connected DCS through controllers 6 & 7 and the
process is operated by 1 Operator Work Station(OWS).
The chips from the silos are fed to the Extruders (JSW) where the polymer chips are
melted at high pressure and made as fine yarn filaments, which is quenched to increase its
strength. The extruders has point temperature, pressure measurements where all instruments
are connected to remote junction boxes to the individual cards connected in the CAN Network
and DeviceNet connects the cards to the OMRON PLC for control. The RTD's are from ozaki
and the pressure transmitters are Nagano Keiki.
Then the chips are extruded into filaments of required denier. This filament, immediately
after extrusion is wound on bobbins after a coat of spin finish oil. This is called undrawn
yarn and given to winders, where it is winded in the bobbins.
TEXTLIES:
The textiles have two stages of product output Twisting Weaving.
The undrawn yarn is stretched about 5 times under elevated temperature conditions to
improve molecular orientation of the yarn in Draw Twisters (DT). This yarn is called drawn
yarn. Here in the DT the temperature is the main process control objective which is sensed
by the RTD’s and controlled individual controllers for each DT, also there are SSR’s for
high speed output isolated switching, MMI for 1&2 and 3&4 DT. The temperature and RH
of the hall is monitored by Abus transmitter and indicated to a local display.
The drawn yarn is twisted in the machine called ply twister in a definite twist per
meter (TPM) in the direction (S) as per the customer requirement. In the machine Cable
Twister double or triple runs of ply twisted yarn are twisted in the opposite (Z) direction. This
product is called Nylon Tyre Cord. Here the length counter of mechanical type is used as
the product length reference.
In the machine called Loom, the Nylon cords are woven into fabric. Here the Nylon
Tyre Cord is the warp and the interlaced cotton yarn used as weft. There are nearly 15
looms and each loom has individual high end control system, the control is carried out by
the CAN bus and OFC, then it has single ended load cells, motorised solenoid valves in
Fixed & Relay nozzles, hand safety sensors, air regulators, length counter, solenoid valves
etc.
DIPPING:
Dipping is the process of coating greige fabric in 40% rubber latex with a solution
of resorcinol and formaldehyde. This process brings about strong adhesion between the rubber
compound (tyre) and the fabric. There are two new driers (1A &1B) of six zones and four old
driers (D1, D2, D3 and D4) of four zones.
Each drier has to maintain the temperature within the specified limits so as to achieve
the product quality, a Siemens S7 PLC acts as master for each unit and also to the sequence
controller. The sequence controller is of ESA-pyronics make which gives appropriate signal
to the step up transformer (for the spark plug) and also gives necessary control signals to the
modulation motor (Gastechnic) and solenoid valves for ignition.
The ignition is sensed by the UV flame sensor (ESA-pyronics) and given to the
sequence controller; also there are pressure switches for sequence operation, such as exhaust
air, fresh air, gas+air switches. Rather than this there are load cells (HBM, E+L etc.) which
are used for the web tension monitoring and control of the PRS motor and rollers. There are
also Sensors for the fabric width adjustments such as Duo canter, Trio canter etc.
UTILITIES:
There are five Fuel Oil Boilers and three Steam Boilers of which one is husk feeding
and other two are oil fired boilers. The husk boiler is of 12 ton capacity and the control loops
are of single loop electronic control. The bed temperature is monitored by the thermocouples
(K- type), the drum level and pressure are measured by the Rosemount (1151 smart)
transmitters, there are pressure switch for pressure safety interlock, mobrey level switch for
level safety interlock, safety relief valves, solenoid valves for sequential bag filter operation.
The SPM analyser is of optical type and used to continuously monitor and record the data’s
this is of Forbes Marshall Codel type installed in the both of the stack.
Effluent treatment Plant will collect all the waste water in and around the plant then
process it by adding chemicals and aerating it and then gives the processed water to the water
treatment plant and the slug to the sewage. There are float type level switches, Magnetic Flow
meters (krohne Marshall) for monitoring flow and a Dissolved oxygen analyser (LDO) Hach
make used to find the oxygen levels in the aerator pond and issues the control signals to the
drives of the blowers so as to control the oxygen levels. The water treatment plant is associated
with RO plant and there are NAMUR types of on/off valves, displacer type of level switches,
E+H Magnetic Flow meters (Promag), Rotameter’ s, pressure switches etc.
There are three Ingersoll Rand (centac) centrifugal 3 stages Compressor’s, three diesel
compressors which are auto start when the pressure in receiver goes down, and kosla
compressors. The inlet and exhaust air flow to the compressor is controlled by the Split range
control action by the microprocessor based controller; also the compressor is associated with
instruments such as vibration sensors, pressure switches, and temperature switches etc., for
control actions.
INTRODUCTION
Purpose:
To provide a suitable industrial experience to an engineering professional with
necessary training in the field of Instrumentation along with TQM, Documentation activities
and SERVICING With high level of knowledge and discipline.
So as to improve the knowledge and skill level with good attitude.
Features:
This training feature in maintenance activities in and around the plant and
documentation work carried out in the Instrumentation Department of SRF Limited-TTBM, a
premier Tyre Cord manufacturing facility in India to understand the realities, infrastructure of
process industries.
To get educated about instruments that are dedicated to measure, monitor, record
and control so as to obtain optimum results. Instruments the heart of every industry which plays
a vital role in the process control applications, especially primary measuring instruments such
as transmitters, sensors, primary sensing elements then control equipment’s such as single loop
controllers, PLC, DCS etc., and bus networks such as FOUNDATION Fieldbus, Profibus,
CAN Bus, Device Net, etc.,
INSTRUMENTATION
Instrumentation is an art of science, which involves measurement,
monitor and control of physical parameters such as pressure, temperature, flow, level, pH etc.
so as to improve product quality to get optimum output. The technology in this field continues
to a rapid development with intelligent electronics and software’s to the instrument systems.
Pressure:
The force per unit area is called the pressure.
We could represent this as:
Pressure = Force / Unit Area
A gauge pressure device will indicate zero pressure when bled down to Atmospheric
pressure.
Absolute pressure includes the effect of atmospheric pressure with the gauge
pressure.
Absolute Pressure = Gauge Pressure + Atmospheric Pressure
The units of measurement are either in pounds per square inch (PSI), kg/cm, Pascal, etc.
Measuring Instrument:
Pressure gauge, Mano meter, pressure transmitter, pressure switch, etc.
Temperature:
Temperature can be defined as degrees of hotness and coldness of an object or a
substance which are expressed according to a comparative scale and shown by a thermometer
or perceived by touch.
The units of measurement are either in degree scale, Celsius, Fahrenheit, kelvin, etc.
Flow:
Flow of a (liquid, gas or electricity) move steadily and continuously process of flowing
any liquid.
Go from one place to another in a steady stream, typically in large numbers.
Flow is directly proportional to the square root of differential pressure created or
caused by (orifice, venture tubes, etc.
Mathematically:
Where,
F – Flow
K – Constant
P1, p2 – DP (differential pressure / sqrt (square root).
The units of measurement are either in m3 per hour, newton, etc.
Measuring Instrument:
Orifice Plate, Rotameter, magnetic flow transmitter, mass flow transmitter, etc.
Differential pressure:
D.P is the pressure between suction pressure between suction pressure and
discharge pressure.
D.P can be created or caused using orifice plates, venturi tubes etc.
Bourdon Tubes Pressure gauge:
Bourdon tubes are circular-shaped tubes with oval cross sections. The pressure
of the medium acts on the inside of the tube. The outward pressure on the oval cross section
forces it to become rounded. Because of the curvature of the tube ring, the bourdon tube then
bends as indicated in the direction of the arrow.
There are different types of bourdon tubes namely type-c, helix, spiral these are all used in
the ways of measuring pressure (depends on the surrounding pressure we use bourdon tubes).
F = k*sqrt [p1-p2]
C – Type bourdon tubes:
Pressure Transmitter:
Produce a linear output proportional to input pressure.
Zero Scale: 3 psi or 4ma.
Full Scale: 15psi or 20 ma.
Most pressure transmitters are built around the pressure capsule concept.
They are usually capable of measuring differential pressure (that is, the Difference between a
high pressure input and a low pressure input) and therefore, are usually called DP transmitters
or DP cells.
A differential pressure capsule is mounted inside a housing. One end of
a force bar is connected to the capsule assembly so that the motion of the capsule can be
transmitted to outside the housing. A sealing mechanism is used where the force bar
penetrates the housing and also acts as the pivot point for the force bar. Provision is made in
the housing for high- pressure fluid to be applied on one side of the capsule and low-pressure
fluid on the other. Any difference in pressure will cause the capsule to deflect and create
motion in the force bar. The top end of the force bar is then connected to a position detector,
which via an electronic system will produce a 4 - 20 ma signal that is proportional to the
force bar movement.
ROTAMETERS:
Rotameter is used to monitor maximum and minimum flow rate of the flow meter.
It is a device that measures the rate of flow of (liquid or gas) in a closed tube.
It belongs to a class of meters called variable area meters, which measures flow
rate by allowing the cross-sectional area the fluid travel and through to vary, causing a
measurable effect.
Rotameter are classified as variable orifice meters.
While fixing it should be vertical due to gravitational force act on the float.
Types of Rotameter:
There are two types of Rotameter they are namely
1. Metal tube
2. Glass tube
Orifice Plate:
The orifice plate is the most common form of restriction that is used in flow
measurement. An orifice plate is basically a thin metal plate with a hole bored in the center or
depends on the types of orifice plates holes are bored in the plate. It has a tab on one side
where the specification of the plate is stamped. The upstream side of the orifice plate usually
has a sharp.
Fixing procedures:
Mostly for gas line diameter weep hole are placed upwards and for oil
lines the weep holes are placed downwards while fixing orifice plates due to venting.
Types of orifice plates:
1- Concentric
2- Segmental
3- Quadrant
4- Eccentric
Concentric:
The concentricorifice plate isusedforideal liquidaswell asgasesand steamservice.Thisorifice
plate betaratiofall betweenof 0.15 to 0.75 for liquidsand0.20 to 0.70 forgases,and steam.Best
resultsoccurbetweenvalue of 0.4and 0.6. Betaratio meansratioof the orifice bore tothe internal
pipe diameters.
Segmental:
The segmental orifice place hasthe hole inthe formsegmentof acircle.Thisisusedfor colloidal and
slurryflowmeasurement.Forbestaccuracy,the tap locationshouldbe 180º fromthe centerof
tangency.
Quadrant Edge:
It commonuse in Europe andare particularlyuseful forpipe sizeslessthan2 inch’s.
Quadrant edge orifices produce a relatively constant coefficient of
discharge for services with low Reynolds numbers in the range from 100,000 down to
5,000.
Eccentric:
The eccentricorifice plate hasa hole eccentric.Use full formeasuringcontainingsolids,oil
containingwaterandwetsteam.Eccentricplatescan use eitherflange orvenacontracttaps, butthe
tap mustbe at 180º or 90º to the eccentricopening.
MASS FLOW METER:
A mass flowmeter,alsoknownas an inertial flowmeter isa device thatmeasures
mass flowrate of a fluidtravelingthroughatube.The massflow rate is the mass of the fluid
travelingpasta fixedpointperunittime
Mass flow meter works under Coriolis principle.
There are two basic configurations of Coriolis flow meter: the curved
tube flow meter and the straight tube flow meter.
The mass flow meter does not measure the volume per unit time (e.g.,
cubic meters per second) passing through the device; it measures the mass per unit time (e.g.,
kilograms per second) flowing through the device. Volumetric flow rate is the mass flow rate
divided by the fluid density. If the density is constant, then the relationship is simple. If the
fluid has varying density, then the relationship is not simple. The density of the fluid may
change with temperature, pressure, or composition, for example. The fluid may also be a
combination of phases such as a fluid with entrained bubbles. Actual density can be
determined due to dependency of sound velocity on the controlled liquid concentration.
THERMOCOUPLES:
Thermocouple means name itself says that thermo means thermal or temperature
and couple means pair join together as thermocouple.
It is also called as seebeck effect because of the person seebeck who invented it.
It is also called as thermo electric effect
A thermocouple consists of two pieces of dissimilar metals with their ends
Joined together (by twisting, soldering or welding). When heat is applied to
the junction, a voltage, in the range of milli-volts (mV), is generated. A
Thermocouple is therefore said to be self-powered or active transducer.
To convert the emf generated by a thermocouple to the standard 4-20 mA
Signal, a transmitter is needed. This kind of transmitter is called a
Temperature transmitter.
There are different types of thermocouple material’s like (K, T, R, J, S, E, V, N, B)
types are used depends on the range of input temperatures it can be choose.
TYPES OF THERMOCOUPLES FOR DIFFERENT TEMPERATURE RANGES:-
Using this above thermocouple chart we can cross check the
thermocouple but for accurate measurement of thermocouple we need to
compensate the room temperature which is acting on the thermocouple that’s the
reason for using diode in the controller’s to compensate room temperature.
Or we can also use ice box techniques near cold junction of
thermocouple for compensation.
RTD:
Resistance Temperature Detectors (RTDs) are temperature sensors that
contain a resistor that changes resistance value as its temperature changes.
They have been used for many years to measure temperature in laboratory
and industrial processes, and have developed a reputation for accuracy,
repeatability, and stability.
There are three wire and four wire rtd’s depends on the length and for more
accuracy they are used.
Thermowell:
The process environment where temperature monitoring is required is often
not only hot, but also pressurized and possibly chemically corrosive or radioactive. To
facilitate removal of the temperature sensors (RTD and TC), for examination or replacement
and to provide mechanical protection, the sensors are usually mounted inside thermal wells.
The most common types of thermowell
Thermowells are commonly classified according to their connection to a process.
The most common types of Thermowells are (1) threaded, (2) socket weld, (3) weld-
in, and (4) flanged.
Level:
The distance between one points to another point is called level.
The units of measurement are either in inch, cm3, meter, etc.
Measuring Instrument:
Level gauge class, DP type transmitter, Displacer transmitter, vibrating fork type
switch, etc.
Many industrial processes require the accurate measurement of fluid or solid
(powder, granule, etc.) height within a vessel. Some process vessels hold a stratified
combination of fluids, naturally separated into different layers by virtue of differing densities,
where the height of the interface point between liquid layers is of interest.
GAUGE GLASSES:
The principle of a gauge glass is that a liquid will tend to seek a
common level as in ‘U’ tube. They are only used for local indication and their reliability is
very important in crosschecking the secondary level instruments. The level gauge or sight
glass is to liquid level measurement as manometers are to pressure measurement: a very
simple and effective technology for direct visual indication of process level. In its simplest
form, a level gauge is nothing more than a clear tube through which process liquid may be
seen. The following photograph shows a simple example of a sight glass.
Differential Pressure method:
Most pressure transmitters are built around the pressure capsule
concept. They are usually capable of measuring differential pressure (that is, the Difference
between a high pressure input and a low pressure input) and therefore, are usually called DP
transmitters or DP cells.
HP is connected to bottom of the tank and LP is connected to top of the closed
tank (if open tank LP is connected to vent area).That HP side acting pressure equal to height
of the tank and density of the liquid. LP side acting vapour pressure.
DP =HP-LP
Displacement type level transmitter:
This works under ARCHIMEDE’S Principle which is (buoyancy force).
The variation in buoyancy resulting from changes liquid level, varies the net
weight of the displacer, increasing or decreasing the load of the torque arm.
The changes is directly proportional to the change in the liquid level.
These level transmitters have major portions of mechanical and pneumatic parts
those are affected by the ambient temperature and pressure.
LVDT:
LVDT is an acronym for Linear Variable Displacement Transducer
LVDT works under the principle of mutual induction, and the displacement
which is a non-electrical energy is converted into an electrical energy.
Turbine Flow meter:
It consist of a turbine (usually four-bladed) placed in the direction of flow.
Within a specified range (flow range usually about 10:1 turndown) the speed of
rotation is directly proportional to flow velocity.
Turbine blades are constructed of ferromagnetic material a pass beneath a magnetic
detector operating as a variable reluctance transducer which produces output voltage
approximately to sin wave of the form.
E = Aw SIN NWT.
Where,
A – constant
W – Angular velocity (proportional to flow velocity)
N – Number of blades
Ultrasonic flow meter:
Ultrasonic flow meter uses Doppler Effect.
Ultrasonic flow meter are ideal for waste water application or any direct
liquid which is conductive or water based;
It will not work with distilled water, also ideal for applications where low
drop, chemical compatibility.
Ultrasonic need only particularities or bubbles in the flow.
Doppler Effect:
It is the change in frequency of a wave for an observer moving relative to its
source.
It is also used for speed measurement in radar speed traps
Doppler flow meter:
Doppler flow meter injects (high frequency typically 100 kilo hertz) sound waves
into moving fluid’s small part of this sound wave is reflected off solid matter, vapor and air
bubbles or eddies / vortices back to a receiver mounted alongside the transmitter.
As it passes through the fluid, the frequency is subject to two changes (one
travelling to upstream against the flow and another one downstream with the flow).
Receivedfrequency:
Doppler flow meter is linear and can be installed without breaking pipes.
FR = FT {(VT + VCOSð) / (VT – VCOSð)}
Hot wire Anemometer:
A Hot wire is inserted in the fluid and maintain at constant temperature
by self-balancing the bridge.
If the flow increases say, more heat is removed, the temperature of the
wire falls and its resistance falls.
This unbalance the bridge, which is detected and the bridge voltage is
increased until the temperature of the wire is restored.
With a constant wire temperature, the heat dissipated by the wire is
equal to the power loss.
I^2 R = A+B SQRT (V)
OR
V = K (I^R – A) ^R
Where k is a constant.
The current I is measured or converted to a voltage by the lower resistor in the bridge)
from which the flow velocity can be delivered, obviously relationship is non-linear and
compensation for changes in fluid temperature is required.
Flow in open channel:
Flow meter in open channels are in supplying and installing radar flow meters for
over 14 years, many of these meters are installed in drains and severs and have never serviced
or even visited after installation and they are still operating perfectly.
Radar will be mounted above the water surface and measure the
flow velocity using RADAR (Radio Detection & Ranging) technology and flow depth using
a level sensor which can be ultrasonic, radar.
The flow rate can be calculated by:
Q = V * A, Accuracy +/- 5%.
Bernoulli’s equation:
Bernoulli’s is used to balance between pressure, velocity and elevation.
Equation:
P+1/2(Þv^2) + þgh = constant
Where,
P – Pressure
Þ – Density
V – Velocity
H – Elevation
G – Gravitational acceleration
State that for an invisid flow of a non – conducting fluid, an
increase in the speed of the fluid occurs simultaneously with a decrease in pressure.
(Increase in velocity then decrease in pressure).
Nucleonic Type Level Transmitter:
NT.L.T operates according to radio-metric principle, utilizing the
physical law that gamma radiation is attenuated as it passes through matter.
Since the source type and the absorption path are constant in this
case, the measure is only affected by the presence of the medium.
All other physical properties such as pressure, temperature, viscosity
and color have no influence.as a consequence, the radiometric measuring method features a
very high level of operational safety and requires partially no maintenance, even under
difficult operating and ambient conditions.
Types of valves:
1. Ball valve
2. Gate valve
3. Global valve
4. Needle valve
5. Mixing valve
6. Diverting valve
7. Butterfly valve
Types of final control elements used in the process industry and their applications:
A control valve essentially comprises of a valve body and an actuator.
Control valve:
A control valve is defined as a power operated device, which modifies the fluid
flow rate in a process control system. It consists of a valve body connected to an actuator
mechanism that is capable of changing the position of a flow-controlling element in the
valve in response to a signal from the controlling system.
Valve body:
A valve body is a device used for the control of fluid flow. It consists of a fluid
retaining assembly; one or more ports between the end opening and a movable closure
member which opens, restricts or closes the port(s).
Actuator:
An actuator is a fluid powered or electrically powered device, which supplies
force and motion to a valve closure member.
Five types of valves:
1. Single seated (ported) globe valve.
2. Double seated (ported) globe valve.
3. Cage type globe valve.
4. Angle valve.
5. Three way globe valves
PROCESS CONTROL
Process control refers to the methods that are used to control process
variables when manufacturing a product. For example, factors such as the proportion of one
ingredient to another, the temperature of the materials, how well the ingredients are mixed,
and the pressure under which the materials are held can significantly impact the quality of an
end product. Manufacturers control the production process for three reasons:
 Reduce variability
 Increase efficiency
 Ensure safety
CONTROL LOOP
OPEN LOOP:
If in a physical system there no automatic correction of the variation in its
output it is called open loop control system. There is no direct measurement of the controlled
variable; its basic is in making an accurate estimate of the form or quantity of action
necessary to accomplish a desired objective.
EXAMPLE:
Gas is fed from source to vesselthrough a valve which is controlled by adjusting the
actuator load pressure (PL)
In order for control system to work, input pressure and flow rate must be maintained as
constant, along with the actuator load pressure. This is because the vesselpressure is not being
measured there is no FEEDBACK.
CLOSED LOOP:
If in a physical system there automatic correction of the variation in its output it
is called closed loop. In general output can be controlled by input through feedback parameters.
PL
GAS
SOURCE
PROCESS
VESSEL
NATURE OF JOB:
 To assist in improvement projects done in and around the plant.
 Quench temperature relocated due to functioning abnormally.
 Dipping plant temperature monitoring and controlling.
 Polymerization plant fixing the DP switch in furnace oil burner (FOB).
 Spinning godet temperate feedback loss monitored and swapped the RTD sensor.
 Mtp plant to replace faulty counter with serviced one.
 In BR & D we used to check temperature and we have a library we used to take some
instrument related notes.
 DT we used to check heating plates with temperature indicator and probe’s.
 If there are temperature diversion below or above set point we do surface correction from
that DT.
 While loading and unloading nitrogen gas in plant we helped technicians.
 In biomass we went to service transreciever and changing temperature sensors and
solenoid valves during shutdown.
 To gain knowledge about process and interlocks related to process instrumentation and
to apply the same.
 To assist in maintenance and troubleshooting activities in day to day basis.
 To gain knowledge and help in ISO documentation.
 To gain knowledge in TQM activities and apply it in daily work.
 To assist in the completion of Preventive Maintenance schedule from Annual Plan on a
monthly basis, and updating Daily Maintenance reports, History cards etc.
 To perform daily activities those have been assigned to us.
Process
Output
Input
Feed back
ELECTRO
NINCS
INSTRU
MENTS
1
ELECTRONIC COUNTER
(LENGTH COUNTER)
YES MTP 55 NOV/FEB ARUN.S(TRAINEE) 82,000
2
VIBRATING FORK LEVEL
SWITCH BOARD (HIGH &
LOW) BOARD'S
YES POLYMERIZATION 15 DEC/FEB ARUN.S(TRAINEE) 22,500
3 SELECT COUNTER YES LOOM 2 MAY ARUN.S(TRAINEE) 4000
4 CONTROLLER YEW UT-350 YES NITROGEN PLANT 1 APRIL ARUN.S(TRAINEE) 20,000
5 FEQUENCY COUNTER YES LOOM 2 JUNE ARUN.S(TRAINEE) 5,000
6 LOAD CELL TESTER YES ASM 1 MAY ARUN.S(TRAINEE) 7,000
7 (DM - 97) MULTIMETER YES INSTRUMENT 2 MAY/JUNE ARUN.S(TRAINEE) 2,000
8
DATA LOG - POWER SUPPLY
CARD
YES LOOM 9 APRIL/MAY ARUN.S(TRAINEE) 13,500
9 RADIX UNIRAD INDICATOR YES DT 1 JUNE ARUN.S(TRAINEE) 2000
10 EWS 15 -9 CARD YES LOOM 1 APRIL ARUN.S(TRAINEE) 5,000
11
HFT - 70 (DIGITAL SURFACE
TEMPERATURE) ANDRITSU
MAKE
YES DT 1 JUNE ARUN.S(TRAINEE) 65,000
12 ELECTRONIC RPM COUNTER YES LOOM 1 FEBRUARY ARUN.S(TRAINEE) 5,000
13
305 THERMOMETER
INDICATOR
YES DT 2 JUNE ARUN.S(TRAINEE) 15,000
14
DIGITAL THERMOMETER
KOMARK MAKE
YES DT 1 JUNE ARUN.S(TRAINEE) 40,000
15 ASM WEIGHING INDICATOR YES SPINNING 2 NOVEMBER ARUN.S(TRAINEE) 40,000
16 LOAD CELL INDICATOR YES POLYMERIZATION 1 FEBRUARY ARUN.S(TRAINEE) 15,000
17 PCB BOARDS YES MTP 20 MAY/JUNE ARUN.S(TRAINEE) 16,000
18 POWER SUPPLY CARD YES DT 2 MAY ARUN.S(TRAINEE) 1,500
19 HOOTER YES DIPPING 1 FEBRUARY ARUN.S(TRAINEE) 5,000
20 AT-CONTROL MODULE YES LOOM 1 AUGUST ARUN.S(TRAINEE) 20,000
21 CA-71 YES
MASTER
INSTRUMENT
1 AUGUST ARUN.S(TRAINEE) 20,000
22 ANEMOMETER YES NITROGEN PLANT 2 DEC/JULY ARUN.S(TRAINEE) 15,000
23 DP PRESSURE SWITCH YES POLYMERIZATION 1 JAN/FEB ARUN.S(TRAINEE) 10,000
24
ACTUATOR SV ("2/3" &
"5/3")
YES NITOGEN PLANT 1 JANUARY ARUN.S(TRAINEE) 7,000
25 DUAL PLUNGER SOV YES NAUTAMIXER 2 APRIL ARUN.S(TRAINEE) 10,000
26 GAS PRESSURE SWITCH YES BIOGAS 1 MARCH ARUN.S(TRAINEE) 3,500
27 LIMIT SWITCH YES DIPPING 2 FEBRUARY ARUN.S(TRAINEE)
28 PRESSURE SWITCH YES SPINNING 5 JAN/FEB ARUN.S(TRAINEE) 5,000
29
PADDLE TYPE LEVEL SWITCH
YES POLYMERIZATION 1 FEBRUARY ARUN.S(TRAINEE) 2,000
30 AIR REGULATORS YES LOOM 9 JAN/MARCH ARUN.S(TRAINEE) 15,000
31 ROTAMETER YES POLYMERIZATION 1 APRIL ARUN.S(TRAINEE) 2,000
32 TEMPERATURE PROBE YES DT 4 JUNE ARUN.S(TRAINEE) 4,000
33 MODULATION MOTOR YES DIPPING 2 DEC/JAN ARUN.S(TRAINEE) 2,00,000
34 SPARK PLUG YES DIPPING 8 DEC/APRIL ARUN.S(TRAINEE) 40,000
37 SOLENOID VALVE YES DEPARTEMENT 8 JAN/MAY ARUN.S(TRAINEE) 15,000
38 LY-25/16 GAS FLOW METER YES LPG BULLET AREA 1 FEBRUARY ARUN.S(TRAINEE) 5,000
39 PRESSURE GUAGE YES PSA TOWER 2 JUNE ARUN.S(TRAINEE)
40
FEEDBACK PRV
YES
OLD POLY ('0'-
MTR)
1 JUNE ARUN.S(TRAINEE) 5,000
41 AIR REGULATORS YES POLYMERIZATION 2 MAY ARUN.S(TRAINEE) 2,000
PRICE
INSTRUMENTS SERVICES IN INSTRUMENTATION DEPARTEMENT UNDER MR.VIVEK SINGH SEGAR PERMISSION
MATERIAL DESCRIPTIONS.NO
TYPE
AREA QUANTITY MONTH SERVICED PERSON
From this above list I saved around 739200 RUPEES only during my
graduate act apprentice period apart from my instrumentation and maintenance work and I am
really thankful for our instrument team members who supported and guided me to do this
wonderful act.
PROJECT INVOLVED
 Calibration bench set up wiring connections and pneumatic connections are
made in our department as per the instruments requirement.
 Biomass automatic bunker conveyer stops using vibrating fork type level
Switch.
 To avoid draw twister heater box surface temperature losing using ANABOND
non insulating conductivity paste.
 Draw twister new temperature control system using delta-v temperature
controller.
 Repairing and servicing electronic and instrument components
CONCLUSION:
In the course of training at SRF Limited- TTBM, I had learnt a lot about this
organization and also about the latest on goings and development in Instrumentation
field. I express my sincere thanks to all the members who have helped directly and
indirectly. Without their help and guidance I wouldn’t have been able to successfully
complete my training worth fully.
ARUN FINAL REPORT

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ARUN FINAL REPORT

  • 1. Final Report GRADUATE ACT. APPRENTICESHIP TRAINING (28Th OCTOBER 2014 – 28Th OCTOBER 2015) S.ARUN Employee No: 600317 B.E & Diploma – ELECTRONICS AND COMMUNICATION ENGINNERING SRF LIMITED – TECHNICALTEXTILESBUSINESS MANALI
  • 2. ACKNOWLEDGEMENT I am immensely grateful to Mr. V. Sekar (Senior Vice President-Operations & complex heads office), SRF LIMITED TTB-Manali, Chennai, for providing the opportunity to get trained and learn in this premier organization. I am immensely thankful to Mr. Narayanan Athmanathan (Deputy General Manager) for providing the opportunity and required facilities. I am immensely thankful to Mr. KALAI SELVAN (Chief Manager) HR for providing the opportunity and required facilities. I express my gratitude and sincere thanks to Mr. VIVEK SINGH SENGAR- Chief Manager (Instrumentation) for his co-operation, invaluable guidance and motivation. I am indebted to [Mr.S.Arunarokiadass, Assistant Manager, Mr.Suvajit Roy, senior Executive] of Instrumentation department, for his invaluable support and supervision throughout the training period, which had kept this training on track. In the course of training at SRF Limited- TTBM, I had learnt a lot about this organization and also about the latest on goings and development in Instrumentation field. I express my sincere thanks to all the members who have helped directly and indirectly. Without their help and guidance I wouldn’t have been able to successfully complete my training worth fully.
  • 3. CERTIFICATE This hereby certify that the work which is being presented for the award of Apprentice Certificate, submitted at SRF Limited, Manali is an authentic record of Mr.S.ARUN carried out under the supervision of Mr. VIVEK SINGH SENGAR, Chief Manager of (Instrumentation). This certification represents excellence in his learning skills also represents his attitude, obedient and sincerely in his work and the way he towards involving himself in mixing up with high standards and self-responsibilities and progress through success and knowledge. He also serviced electronics’ and instrument’s which are added in the list. This is to certify that the above statement made by the candidate is correct to the best of my knowledge. (Mr. Vivek Singh Sengar) Chief Manager - Instrumentation SRF Limited-TTBM Chennai – 600068.
  • 4. SRF LIMITED PROFILE: The SRF is a multi-business entity engaged in the manufacturing of chemical based industrial intermediates. Established in 1973, SRF has today grown into a global enterprise with operations in 4 countries. With headquarters in Gurgaon, India, the $450 million company has operations in three more countries, UAE, Thailand and South Africa. Apart from Technical Textiles Business, in which it enjoys a global leadership position, SRF is a domestic leader in Refrigerants, Engineering Plastics and Industrial Yarns as well. The company also enjoys a significant presence among the key domestic manufacturers of Polyester Films and Fluorospecialities. Building on its in-house R&D facilities for Technical Textiles Business and Chemicals Business, the company strives to stay ahead in business through innovations in operations and product development. A winner of the prestigious Deming Application Prize for its tyre cord business, SRF continues to redefine its work and corporate culture with the TQM as its management way. SRF Today - a snapshot  Rs. 2000 crore multi-product, multi-business organizations.  Market leader in Technical Textiles, Refrigerants, Engineering Plastics and Industrial Yarns.  Manufacturing plants spread over 8 locations in India, one in Dubai, one in South Africa and one in Thailand.  World's 2nd largest producer of Nylon 6 tyre cord fabrics.  World's 2nd largest producer of belting fabrics.  Exporting to over 60 countries.
  • 5. Process Overview Capro Lactam Chips Yarn Undipped Fabric Molten Lactam Additives Ply Dipped Fabric Polymer Polymer Cord Tyre Cord fabric Chips Yarn Fabric Polymerization Dipping Spinning Twisting and Loom
  • 6. NEW YARN PLANT - POLYMERIZATION: The NYP Ploy plant is the first stage, where the raw material “caprolactam” is fed, treated at confined conditions then made into polymer and pelletized into polymer chips stored in the silos. Instrumentation plays a vital role in this plant with high end technology, because the plant uses most of the transmitters and control valves of “FOUNDATION Fieldbus” technology; which is all digital, duplex, self-diagnostics and multidrop technology and “Profibus” for drives with “DELTA V” DCS. Also it uses conventional on/off valves, temperature sensing elements etc. The temperature in the entire process should be maintained at the specified limits and the product should not be oxidized, so as to maintain the quality of the final product. The entire process involves mainly closed loops which are feedback type; also the process has multiple interlocks for safe operation. The entire plant is controlled by three DELTA V MD controllers (1, 2, 3) where controller 1 is assigned to discrete instruments, controller 2 is assigned to analog instruments and the controller is assigned to De-Polymerization area. The entire plant is operated by 2 Operator Work Stations (OWS), which is controlled by a Professional plus station (DVINST).
  • 7. The process parameters such as pressure, level and DP flow where measured using the Rosemount 3051(FF) type transmitters and Yokogawa D-Harp type etc. Mass flow is measured using the multi parameter measuring Micro Motion F-series (FF) Coriolis sensors and 2700 Micro Motion transmitters. The magnetic flow meters are of Rosemount 8742C (FF)Most of the control valves are of Samson 3730-5 (FF) make. The point level is measured using vibrating fork and capacitance type level switches of Sapcon make, and uses temperature sensors such as PT100, K type thermocouples and also other instruments such Trace Oxygen analysers, Solenoid valves, Rotameter’ s etc.,. NEW YARN PLANT - SPINNING: The NYP Spinning is the second stage of the process, where the polymer chips mixed with CUI then heated and melted at specified temperature and pressure then quenched and made into fine filaments of yarn and rolled up in the bobbins. The plant is in technical collaboration with TMT Machinery Co, Japan. There are four chip receiving silos, the chips from the silos in poly are transferred to the nine unit’s CRS1 through the Nitrogen pressure and it is incorporated with vibrating fork level switches so as to indicate the level. Then the chips are mixed in 20(Chips):4(CUI) ratio
  • 8. in the ASM area which is controlled by a Siemens S7 PLC, the inputs and outputs are connected to the DCS through the Remote I/O sub-system 1. The load in the hoppers are measured by load cells A-stuff (S type), B-stuff (Single Ended) then mixed and fed to CRS 2.the CRS 2 & 3 are maintained at below atmospheric pressure. Also these silos have pressure switches, gauges, vibrating fork level switches and solenoid valves etc. which are connected to the DCS through the Remote I/O sub-system 2 and connected DCS through controllers 6 & 7 and the process is operated by 1 Operator Work Station(OWS). The chips from the silos are fed to the Extruders (JSW) where the polymer chips are melted at high pressure and made as fine yarn filaments, which is quenched to increase its strength. The extruders has point temperature, pressure measurements where all instruments are connected to remote junction boxes to the individual cards connected in the CAN Network and DeviceNet connects the cards to the OMRON PLC for control. The RTD's are from ozaki and the pressure transmitters are Nagano Keiki. Then the chips are extruded into filaments of required denier. This filament, immediately after extrusion is wound on bobbins after a coat of spin finish oil. This is called undrawn yarn and given to winders, where it is winded in the bobbins. TEXTLIES: The textiles have two stages of product output Twisting Weaving. The undrawn yarn is stretched about 5 times under elevated temperature conditions to improve molecular orientation of the yarn in Draw Twisters (DT). This yarn is called drawn yarn. Here in the DT the temperature is the main process control objective which is sensed by the RTD’s and controlled individual controllers for each DT, also there are SSR’s for high speed output isolated switching, MMI for 1&2 and 3&4 DT. The temperature and RH of the hall is monitored by Abus transmitter and indicated to a local display. The drawn yarn is twisted in the machine called ply twister in a definite twist per meter (TPM) in the direction (S) as per the customer requirement. In the machine Cable Twister double or triple runs of ply twisted yarn are twisted in the opposite (Z) direction. This product is called Nylon Tyre Cord. Here the length counter of mechanical type is used as the product length reference. In the machine called Loom, the Nylon cords are woven into fabric. Here the Nylon Tyre Cord is the warp and the interlaced cotton yarn used as weft. There are nearly 15
  • 9. looms and each loom has individual high end control system, the control is carried out by the CAN bus and OFC, then it has single ended load cells, motorised solenoid valves in Fixed & Relay nozzles, hand safety sensors, air regulators, length counter, solenoid valves etc. DIPPING: Dipping is the process of coating greige fabric in 40% rubber latex with a solution of resorcinol and formaldehyde. This process brings about strong adhesion between the rubber compound (tyre) and the fabric. There are two new driers (1A &1B) of six zones and four old driers (D1, D2, D3 and D4) of four zones. Each drier has to maintain the temperature within the specified limits so as to achieve the product quality, a Siemens S7 PLC acts as master for each unit and also to the sequence controller. The sequence controller is of ESA-pyronics make which gives appropriate signal to the step up transformer (for the spark plug) and also gives necessary control signals to the modulation motor (Gastechnic) and solenoid valves for ignition. The ignition is sensed by the UV flame sensor (ESA-pyronics) and given to the sequence controller; also there are pressure switches for sequence operation, such as exhaust air, fresh air, gas+air switches. Rather than this there are load cells (HBM, E+L etc.) which
  • 10. are used for the web tension monitoring and control of the PRS motor and rollers. There are also Sensors for the fabric width adjustments such as Duo canter, Trio canter etc. UTILITIES: There are five Fuel Oil Boilers and three Steam Boilers of which one is husk feeding and other two are oil fired boilers. The husk boiler is of 12 ton capacity and the control loops are of single loop electronic control. The bed temperature is monitored by the thermocouples (K- type), the drum level and pressure are measured by the Rosemount (1151 smart) transmitters, there are pressure switch for pressure safety interlock, mobrey level switch for level safety interlock, safety relief valves, solenoid valves for sequential bag filter operation. The SPM analyser is of optical type and used to continuously monitor and record the data’s this is of Forbes Marshall Codel type installed in the both of the stack. Effluent treatment Plant will collect all the waste water in and around the plant then process it by adding chemicals and aerating it and then gives the processed water to the water treatment plant and the slug to the sewage. There are float type level switches, Magnetic Flow meters (krohne Marshall) for monitoring flow and a Dissolved oxygen analyser (LDO) Hach make used to find the oxygen levels in the aerator pond and issues the control signals to the drives of the blowers so as to control the oxygen levels. The water treatment plant is associated with RO plant and there are NAMUR types of on/off valves, displacer type of level switches, E+H Magnetic Flow meters (Promag), Rotameter’ s, pressure switches etc. There are three Ingersoll Rand (centac) centrifugal 3 stages Compressor’s, three diesel compressors which are auto start when the pressure in receiver goes down, and kosla compressors. The inlet and exhaust air flow to the compressor is controlled by the Split range control action by the microprocessor based controller; also the compressor is associated with instruments such as vibration sensors, pressure switches, and temperature switches etc., for control actions.
  • 11. INTRODUCTION Purpose: To provide a suitable industrial experience to an engineering professional with necessary training in the field of Instrumentation along with TQM, Documentation activities and SERVICING With high level of knowledge and discipline. So as to improve the knowledge and skill level with good attitude. Features: This training feature in maintenance activities in and around the plant and documentation work carried out in the Instrumentation Department of SRF Limited-TTBM, a premier Tyre Cord manufacturing facility in India to understand the realities, infrastructure of process industries. To get educated about instruments that are dedicated to measure, monitor, record and control so as to obtain optimum results. Instruments the heart of every industry which plays a vital role in the process control applications, especially primary measuring instruments such as transmitters, sensors, primary sensing elements then control equipment’s such as single loop controllers, PLC, DCS etc., and bus networks such as FOUNDATION Fieldbus, Profibus, CAN Bus, Device Net, etc.,
  • 12. INSTRUMENTATION Instrumentation is an art of science, which involves measurement, monitor and control of physical parameters such as pressure, temperature, flow, level, pH etc. so as to improve product quality to get optimum output. The technology in this field continues to a rapid development with intelligent electronics and software’s to the instrument systems. Pressure: The force per unit area is called the pressure. We could represent this as: Pressure = Force / Unit Area A gauge pressure device will indicate zero pressure when bled down to Atmospheric pressure. Absolute pressure includes the effect of atmospheric pressure with the gauge pressure. Absolute Pressure = Gauge Pressure + Atmospheric Pressure The units of measurement are either in pounds per square inch (PSI), kg/cm, Pascal, etc. Measuring Instrument: Pressure gauge, Mano meter, pressure transmitter, pressure switch, etc. Temperature: Temperature can be defined as degrees of hotness and coldness of an object or a substance which are expressed according to a comparative scale and shown by a thermometer or perceived by touch. The units of measurement are either in degree scale, Celsius, Fahrenheit, kelvin, etc.
  • 13. Flow: Flow of a (liquid, gas or electricity) move steadily and continuously process of flowing any liquid. Go from one place to another in a steady stream, typically in large numbers. Flow is directly proportional to the square root of differential pressure created or caused by (orifice, venture tubes, etc. Mathematically: Where, F – Flow K – Constant P1, p2 – DP (differential pressure / sqrt (square root). The units of measurement are either in m3 per hour, newton, etc. Measuring Instrument: Orifice Plate, Rotameter, magnetic flow transmitter, mass flow transmitter, etc. Differential pressure: D.P is the pressure between suction pressure between suction pressure and discharge pressure. D.P can be created or caused using orifice plates, venturi tubes etc. Bourdon Tubes Pressure gauge: Bourdon tubes are circular-shaped tubes with oval cross sections. The pressure of the medium acts on the inside of the tube. The outward pressure on the oval cross section forces it to become rounded. Because of the curvature of the tube ring, the bourdon tube then bends as indicated in the direction of the arrow. There are different types of bourdon tubes namely type-c, helix, spiral these are all used in the ways of measuring pressure (depends on the surrounding pressure we use bourdon tubes). F = k*sqrt [p1-p2]
  • 14. C – Type bourdon tubes: Pressure Transmitter: Produce a linear output proportional to input pressure. Zero Scale: 3 psi or 4ma. Full Scale: 15psi or 20 ma. Most pressure transmitters are built around the pressure capsule concept. They are usually capable of measuring differential pressure (that is, the Difference between a high pressure input and a low pressure input) and therefore, are usually called DP transmitters or DP cells. A differential pressure capsule is mounted inside a housing. One end of a force bar is connected to the capsule assembly so that the motion of the capsule can be transmitted to outside the housing. A sealing mechanism is used where the force bar penetrates the housing and also acts as the pivot point for the force bar. Provision is made in the housing for high- pressure fluid to be applied on one side of the capsule and low-pressure
  • 15. fluid on the other. Any difference in pressure will cause the capsule to deflect and create motion in the force bar. The top end of the force bar is then connected to a position detector, which via an electronic system will produce a 4 - 20 ma signal that is proportional to the force bar movement. ROTAMETERS: Rotameter is used to monitor maximum and minimum flow rate of the flow meter. It is a device that measures the rate of flow of (liquid or gas) in a closed tube. It belongs to a class of meters called variable area meters, which measures flow rate by allowing the cross-sectional area the fluid travel and through to vary, causing a measurable effect. Rotameter are classified as variable orifice meters. While fixing it should be vertical due to gravitational force act on the float. Types of Rotameter: There are two types of Rotameter they are namely 1. Metal tube 2. Glass tube
  • 16. Orifice Plate: The orifice plate is the most common form of restriction that is used in flow measurement. An orifice plate is basically a thin metal plate with a hole bored in the center or depends on the types of orifice plates holes are bored in the plate. It has a tab on one side where the specification of the plate is stamped. The upstream side of the orifice plate usually has a sharp. Fixing procedures: Mostly for gas line diameter weep hole are placed upwards and for oil lines the weep holes are placed downwards while fixing orifice plates due to venting. Types of orifice plates: 1- Concentric 2- Segmental 3- Quadrant 4- Eccentric Concentric: The concentricorifice plate isusedforideal liquidaswell asgasesand steamservice.Thisorifice plate betaratiofall betweenof 0.15 to 0.75 for liquidsand0.20 to 0.70 forgases,and steam.Best resultsoccurbetweenvalue of 0.4and 0.6. Betaratio meansratioof the orifice bore tothe internal pipe diameters.
  • 17. Segmental: The segmental orifice place hasthe hole inthe formsegmentof acircle.Thisisusedfor colloidal and slurryflowmeasurement.Forbestaccuracy,the tap locationshouldbe 180º fromthe centerof tangency. Quadrant Edge: It commonuse in Europe andare particularlyuseful forpipe sizeslessthan2 inch’s. Quadrant edge orifices produce a relatively constant coefficient of discharge for services with low Reynolds numbers in the range from 100,000 down to 5,000. Eccentric: The eccentricorifice plate hasa hole eccentric.Use full formeasuringcontainingsolids,oil containingwaterandwetsteam.Eccentricplatescan use eitherflange orvenacontracttaps, butthe tap mustbe at 180º or 90º to the eccentricopening. MASS FLOW METER: A mass flowmeter,alsoknownas an inertial flowmeter isa device thatmeasures mass flowrate of a fluidtravelingthroughatube.The massflow rate is the mass of the fluid travelingpasta fixedpointperunittime
  • 18. Mass flow meter works under Coriolis principle. There are two basic configurations of Coriolis flow meter: the curved tube flow meter and the straight tube flow meter. The mass flow meter does not measure the volume per unit time (e.g., cubic meters per second) passing through the device; it measures the mass per unit time (e.g., kilograms per second) flowing through the device. Volumetric flow rate is the mass flow rate divided by the fluid density. If the density is constant, then the relationship is simple. If the fluid has varying density, then the relationship is not simple. The density of the fluid may change with temperature, pressure, or composition, for example. The fluid may also be a combination of phases such as a fluid with entrained bubbles. Actual density can be determined due to dependency of sound velocity on the controlled liquid concentration. THERMOCOUPLES: Thermocouple means name itself says that thermo means thermal or temperature and couple means pair join together as thermocouple. It is also called as seebeck effect because of the person seebeck who invented it. It is also called as thermo electric effect A thermocouple consists of two pieces of dissimilar metals with their ends Joined together (by twisting, soldering or welding). When heat is applied to the junction, a voltage, in the range of milli-volts (mV), is generated. A Thermocouple is therefore said to be self-powered or active transducer. To convert the emf generated by a thermocouple to the standard 4-20 mA Signal, a transmitter is needed. This kind of transmitter is called a Temperature transmitter. There are different types of thermocouple material’s like (K, T, R, J, S, E, V, N, B) types are used depends on the range of input temperatures it can be choose.
  • 19. TYPES OF THERMOCOUPLES FOR DIFFERENT TEMPERATURE RANGES:- Using this above thermocouple chart we can cross check the thermocouple but for accurate measurement of thermocouple we need to compensate the room temperature which is acting on the thermocouple that’s the reason for using diode in the controller’s to compensate room temperature. Or we can also use ice box techniques near cold junction of thermocouple for compensation.
  • 20. RTD: Resistance Temperature Detectors (RTDs) are temperature sensors that contain a resistor that changes resistance value as its temperature changes. They have been used for many years to measure temperature in laboratory and industrial processes, and have developed a reputation for accuracy, repeatability, and stability. There are three wire and four wire rtd’s depends on the length and for more accuracy they are used. Thermowell: The process environment where temperature monitoring is required is often not only hot, but also pressurized and possibly chemically corrosive or radioactive. To facilitate removal of the temperature sensors (RTD and TC), for examination or replacement and to provide mechanical protection, the sensors are usually mounted inside thermal wells. The most common types of thermowell Thermowells are commonly classified according to their connection to a process. The most common types of Thermowells are (1) threaded, (2) socket weld, (3) weld- in, and (4) flanged.
  • 21. Level: The distance between one points to another point is called level. The units of measurement are either in inch, cm3, meter, etc. Measuring Instrument: Level gauge class, DP type transmitter, Displacer transmitter, vibrating fork type switch, etc. Many industrial processes require the accurate measurement of fluid or solid (powder, granule, etc.) height within a vessel. Some process vessels hold a stratified combination of fluids, naturally separated into different layers by virtue of differing densities, where the height of the interface point between liquid layers is of interest. GAUGE GLASSES: The principle of a gauge glass is that a liquid will tend to seek a common level as in ‘U’ tube. They are only used for local indication and their reliability is very important in crosschecking the secondary level instruments. The level gauge or sight glass is to liquid level measurement as manometers are to pressure measurement: a very simple and effective technology for direct visual indication of process level. In its simplest form, a level gauge is nothing more than a clear tube through which process liquid may be seen. The following photograph shows a simple example of a sight glass.
  • 22. Differential Pressure method: Most pressure transmitters are built around the pressure capsule concept. They are usually capable of measuring differential pressure (that is, the Difference between a high pressure input and a low pressure input) and therefore, are usually called DP transmitters or DP cells. HP is connected to bottom of the tank and LP is connected to top of the closed tank (if open tank LP is connected to vent area).That HP side acting pressure equal to height of the tank and density of the liquid. LP side acting vapour pressure. DP =HP-LP Displacement type level transmitter: This works under ARCHIMEDE’S Principle which is (buoyancy force). The variation in buoyancy resulting from changes liquid level, varies the net weight of the displacer, increasing or decreasing the load of the torque arm. The changes is directly proportional to the change in the liquid level. These level transmitters have major portions of mechanical and pneumatic parts those are affected by the ambient temperature and pressure.
  • 23. LVDT: LVDT is an acronym for Linear Variable Displacement Transducer LVDT works under the principle of mutual induction, and the displacement which is a non-electrical energy is converted into an electrical energy. Turbine Flow meter: It consist of a turbine (usually four-bladed) placed in the direction of flow. Within a specified range (flow range usually about 10:1 turndown) the speed of rotation is directly proportional to flow velocity. Turbine blades are constructed of ferromagnetic material a pass beneath a magnetic detector operating as a variable reluctance transducer which produces output voltage approximately to sin wave of the form.
  • 24. E = Aw SIN NWT. Where, A – constant W – Angular velocity (proportional to flow velocity) N – Number of blades Ultrasonic flow meter: Ultrasonic flow meter uses Doppler Effect. Ultrasonic flow meter are ideal for waste water application or any direct liquid which is conductive or water based; It will not work with distilled water, also ideal for applications where low drop, chemical compatibility. Ultrasonic need only particularities or bubbles in the flow.
  • 25. Doppler Effect: It is the change in frequency of a wave for an observer moving relative to its source. It is also used for speed measurement in radar speed traps Doppler flow meter: Doppler flow meter injects (high frequency typically 100 kilo hertz) sound waves into moving fluid’s small part of this sound wave is reflected off solid matter, vapor and air bubbles or eddies / vortices back to a receiver mounted alongside the transmitter. As it passes through the fluid, the frequency is subject to two changes (one travelling to upstream against the flow and another one downstream with the flow). Receivedfrequency: Doppler flow meter is linear and can be installed without breaking pipes. FR = FT {(VT + VCOSð) / (VT – VCOSð)}
  • 26. Hot wire Anemometer: A Hot wire is inserted in the fluid and maintain at constant temperature by self-balancing the bridge. If the flow increases say, more heat is removed, the temperature of the wire falls and its resistance falls. This unbalance the bridge, which is detected and the bridge voltage is increased until the temperature of the wire is restored. With a constant wire temperature, the heat dissipated by the wire is equal to the power loss. I^2 R = A+B SQRT (V) OR V = K (I^R – A) ^R Where k is a constant. The current I is measured or converted to a voltage by the lower resistor in the bridge) from which the flow velocity can be delivered, obviously relationship is non-linear and compensation for changes in fluid temperature is required.
  • 27. Flow in open channel: Flow meter in open channels are in supplying and installing radar flow meters for over 14 years, many of these meters are installed in drains and severs and have never serviced or even visited after installation and they are still operating perfectly. Radar will be mounted above the water surface and measure the flow velocity using RADAR (Radio Detection & Ranging) technology and flow depth using a level sensor which can be ultrasonic, radar. The flow rate can be calculated by: Q = V * A, Accuracy +/- 5%.
  • 28. Bernoulli’s equation: Bernoulli’s is used to balance between pressure, velocity and elevation. Equation: P+1/2(Þv^2) + þgh = constant Where, P – Pressure Þ – Density V – Velocity H – Elevation G – Gravitational acceleration State that for an invisid flow of a non – conducting fluid, an increase in the speed of the fluid occurs simultaneously with a decrease in pressure. (Increase in velocity then decrease in pressure). Nucleonic Type Level Transmitter: NT.L.T operates according to radio-metric principle, utilizing the physical law that gamma radiation is attenuated as it passes through matter. Since the source type and the absorption path are constant in this case, the measure is only affected by the presence of the medium.
  • 29. All other physical properties such as pressure, temperature, viscosity and color have no influence.as a consequence, the radiometric measuring method features a very high level of operational safety and requires partially no maintenance, even under difficult operating and ambient conditions. Types of valves: 1. Ball valve 2. Gate valve 3. Global valve 4. Needle valve 5. Mixing valve 6. Diverting valve 7. Butterfly valve Types of final control elements used in the process industry and their applications: A control valve essentially comprises of a valve body and an actuator. Control valve: A control valve is defined as a power operated device, which modifies the fluid flow rate in a process control system. It consists of a valve body connected to an actuator mechanism that is capable of changing the position of a flow-controlling element in the valve in response to a signal from the controlling system. Valve body: A valve body is a device used for the control of fluid flow. It consists of a fluid retaining assembly; one or more ports between the end opening and a movable closure member which opens, restricts or closes the port(s). Actuator: An actuator is a fluid powered or electrically powered device, which supplies force and motion to a valve closure member.
  • 30. Five types of valves: 1. Single seated (ported) globe valve. 2. Double seated (ported) globe valve. 3. Cage type globe valve. 4. Angle valve. 5. Three way globe valves PROCESS CONTROL Process control refers to the methods that are used to control process variables when manufacturing a product. For example, factors such as the proportion of one ingredient to another, the temperature of the materials, how well the ingredients are mixed, and the pressure under which the materials are held can significantly impact the quality of an end product. Manufacturers control the production process for three reasons:  Reduce variability  Increase efficiency  Ensure safety CONTROL LOOP OPEN LOOP: If in a physical system there no automatic correction of the variation in its output it is called open loop control system. There is no direct measurement of the controlled variable; its basic is in making an accurate estimate of the form or quantity of action necessary to accomplish a desired objective. EXAMPLE: Gas is fed from source to vesselthrough a valve which is controlled by adjusting the actuator load pressure (PL) In order for control system to work, input pressure and flow rate must be maintained as constant, along with the actuator load pressure. This is because the vesselpressure is not being measured there is no FEEDBACK. CLOSED LOOP: If in a physical system there automatic correction of the variation in its output it is called closed loop. In general output can be controlled by input through feedback parameters. PL GAS SOURCE PROCESS VESSEL
  • 31. NATURE OF JOB:  To assist in improvement projects done in and around the plant.  Quench temperature relocated due to functioning abnormally.  Dipping plant temperature monitoring and controlling.  Polymerization plant fixing the DP switch in furnace oil burner (FOB).  Spinning godet temperate feedback loss monitored and swapped the RTD sensor.  Mtp plant to replace faulty counter with serviced one.  In BR & D we used to check temperature and we have a library we used to take some instrument related notes.  DT we used to check heating plates with temperature indicator and probe’s.  If there are temperature diversion below or above set point we do surface correction from that DT.  While loading and unloading nitrogen gas in plant we helped technicians.  In biomass we went to service transreciever and changing temperature sensors and solenoid valves during shutdown.  To gain knowledge about process and interlocks related to process instrumentation and to apply the same.  To assist in maintenance and troubleshooting activities in day to day basis.  To gain knowledge and help in ISO documentation.  To gain knowledge in TQM activities and apply it in daily work.  To assist in the completion of Preventive Maintenance schedule from Annual Plan on a monthly basis, and updating Daily Maintenance reports, History cards etc.  To perform daily activities those have been assigned to us. Process Output Input Feed back
  • 32. ELECTRO NINCS INSTRU MENTS 1 ELECTRONIC COUNTER (LENGTH COUNTER) YES MTP 55 NOV/FEB ARUN.S(TRAINEE) 82,000 2 VIBRATING FORK LEVEL SWITCH BOARD (HIGH & LOW) BOARD'S YES POLYMERIZATION 15 DEC/FEB ARUN.S(TRAINEE) 22,500 3 SELECT COUNTER YES LOOM 2 MAY ARUN.S(TRAINEE) 4000 4 CONTROLLER YEW UT-350 YES NITROGEN PLANT 1 APRIL ARUN.S(TRAINEE) 20,000 5 FEQUENCY COUNTER YES LOOM 2 JUNE ARUN.S(TRAINEE) 5,000 6 LOAD CELL TESTER YES ASM 1 MAY ARUN.S(TRAINEE) 7,000 7 (DM - 97) MULTIMETER YES INSTRUMENT 2 MAY/JUNE ARUN.S(TRAINEE) 2,000 8 DATA LOG - POWER SUPPLY CARD YES LOOM 9 APRIL/MAY ARUN.S(TRAINEE) 13,500 9 RADIX UNIRAD INDICATOR YES DT 1 JUNE ARUN.S(TRAINEE) 2000 10 EWS 15 -9 CARD YES LOOM 1 APRIL ARUN.S(TRAINEE) 5,000 11 HFT - 70 (DIGITAL SURFACE TEMPERATURE) ANDRITSU MAKE YES DT 1 JUNE ARUN.S(TRAINEE) 65,000 12 ELECTRONIC RPM COUNTER YES LOOM 1 FEBRUARY ARUN.S(TRAINEE) 5,000 13 305 THERMOMETER INDICATOR YES DT 2 JUNE ARUN.S(TRAINEE) 15,000 14 DIGITAL THERMOMETER KOMARK MAKE YES DT 1 JUNE ARUN.S(TRAINEE) 40,000 15 ASM WEIGHING INDICATOR YES SPINNING 2 NOVEMBER ARUN.S(TRAINEE) 40,000 16 LOAD CELL INDICATOR YES POLYMERIZATION 1 FEBRUARY ARUN.S(TRAINEE) 15,000 17 PCB BOARDS YES MTP 20 MAY/JUNE ARUN.S(TRAINEE) 16,000 18 POWER SUPPLY CARD YES DT 2 MAY ARUN.S(TRAINEE) 1,500 19 HOOTER YES DIPPING 1 FEBRUARY ARUN.S(TRAINEE) 5,000 20 AT-CONTROL MODULE YES LOOM 1 AUGUST ARUN.S(TRAINEE) 20,000 21 CA-71 YES MASTER INSTRUMENT 1 AUGUST ARUN.S(TRAINEE) 20,000 22 ANEMOMETER YES NITROGEN PLANT 2 DEC/JULY ARUN.S(TRAINEE) 15,000 23 DP PRESSURE SWITCH YES POLYMERIZATION 1 JAN/FEB ARUN.S(TRAINEE) 10,000 24 ACTUATOR SV ("2/3" & "5/3") YES NITOGEN PLANT 1 JANUARY ARUN.S(TRAINEE) 7,000 25 DUAL PLUNGER SOV YES NAUTAMIXER 2 APRIL ARUN.S(TRAINEE) 10,000 26 GAS PRESSURE SWITCH YES BIOGAS 1 MARCH ARUN.S(TRAINEE) 3,500 27 LIMIT SWITCH YES DIPPING 2 FEBRUARY ARUN.S(TRAINEE) 28 PRESSURE SWITCH YES SPINNING 5 JAN/FEB ARUN.S(TRAINEE) 5,000 29 PADDLE TYPE LEVEL SWITCH YES POLYMERIZATION 1 FEBRUARY ARUN.S(TRAINEE) 2,000 30 AIR REGULATORS YES LOOM 9 JAN/MARCH ARUN.S(TRAINEE) 15,000 31 ROTAMETER YES POLYMERIZATION 1 APRIL ARUN.S(TRAINEE) 2,000 32 TEMPERATURE PROBE YES DT 4 JUNE ARUN.S(TRAINEE) 4,000 33 MODULATION MOTOR YES DIPPING 2 DEC/JAN ARUN.S(TRAINEE) 2,00,000 34 SPARK PLUG YES DIPPING 8 DEC/APRIL ARUN.S(TRAINEE) 40,000 37 SOLENOID VALVE YES DEPARTEMENT 8 JAN/MAY ARUN.S(TRAINEE) 15,000 38 LY-25/16 GAS FLOW METER YES LPG BULLET AREA 1 FEBRUARY ARUN.S(TRAINEE) 5,000 39 PRESSURE GUAGE YES PSA TOWER 2 JUNE ARUN.S(TRAINEE) 40 FEEDBACK PRV YES OLD POLY ('0'- MTR) 1 JUNE ARUN.S(TRAINEE) 5,000 41 AIR REGULATORS YES POLYMERIZATION 2 MAY ARUN.S(TRAINEE) 2,000 PRICE INSTRUMENTS SERVICES IN INSTRUMENTATION DEPARTEMENT UNDER MR.VIVEK SINGH SEGAR PERMISSION MATERIAL DESCRIPTIONS.NO TYPE AREA QUANTITY MONTH SERVICED PERSON
  • 33. From this above list I saved around 739200 RUPEES only during my graduate act apprentice period apart from my instrumentation and maintenance work and I am really thankful for our instrument team members who supported and guided me to do this wonderful act. PROJECT INVOLVED  Calibration bench set up wiring connections and pneumatic connections are made in our department as per the instruments requirement.  Biomass automatic bunker conveyer stops using vibrating fork type level Switch.  To avoid draw twister heater box surface temperature losing using ANABOND non insulating conductivity paste.  Draw twister new temperature control system using delta-v temperature controller.  Repairing and servicing electronic and instrument components CONCLUSION: In the course of training at SRF Limited- TTBM, I had learnt a lot about this organization and also about the latest on goings and development in Instrumentation field. I express my sincere thanks to all the members who have helped directly and indirectly. Without their help and guidance I wouldn’t have been able to successfully complete my training worth fully.