Gujrat Technical university
Laxmi Instute of Technology
Sarigam Valsad
Prepared By
Vipendra Kumar
220863119015
CONTENTS
• Internship Details
• Objectives
• Introduction
•
• Brief About Aarti Industry
• Production Range
• Utility Maintenance
• Water treatment plant
• Outcomes
• Conclusions
Objectives
Technical Objectives :
1. Gain improvement in SAP system.
2 . Learn industry-based standard practices like kaizen and 5S" activity.
Soft Skill Objectives:
1 . Improving communication and presentation skills.
2. Learn problem solving and thunking abilities.
Personal Growth Objectives :
1 . Contribute to the compnay and its goals.
2 . Gain valuable industry experience and build a professional work.
3 . Gain Knowledge industry working culture and gain experience equipments.
Internship Details
• Company Name - Aarti Industries LTD Vapi
• External Guide - Sudhir Gupta
• Internal Guide - Hemant Patel
• Department - Utility Maintenance / Engg. Department
• Role : intern/ Trainee
• Location: Vapi
• From : 19/03/2025 to 19/04/2025
• Working Hour : 09:00 AM To 17:30 PM
Chapter 1 : Introduction
Introduction
Acid Division Apple Devision
Fertilizer
Organic
Devi
sion
Necent Division
Amine
De
vis
ion
Different Chemical Under Aarti Industry
SULFURIC ACID LIQUID SO3 DI-METHYLE SULPHATE
PNCB CSA OLEUM
DCB GYPSUM DCP
NITRO BENZENE HYDROCHLORIC ACID NITRIC ACID
Chapter 2 : Utility Maintenance
(Chilling Plant)
Introduction of Chilling plant
Chiiling Plant Cappicity : 60 TR
Refrigrerant Name : 134A
COMPRESSOR TYPE : Dual srew compressor
Condensor Type : Water shell and tube type Condensor
Evoporator Type : Shell and Tube type
Hot and Cold Well : 30 M2 Area
Insulation type : Nitraile type cold insulation ( thick ness - 50 mm)
Insulation Density : 60 mm
Chilling water outlet Temp. : 7 deree celcius
Chilling water inlet Temp. : 12 degree celceus
Cooling tower cappicity : 100 TR
Primary circulation pump : 35 m3/hr
Secondary circulation pump : 35 m3/hr
Chilling Plant cycle
Chiiling plant working
Chiller plant works by using a refrigeration cycle to transfer heat from a sou
rce (like chilled water) to a heat sink (like cooling tower or air). This proc
ess involves a refrigerant that undergoes phase changes (liquid to vapor
and back), absorbing and releasing heat along the way.
Chilling plant Main Four Components are bellow ;
1. Evaporation:
Liquid refrigerant enters the evaporator (a heat exchanger).
Heat is extracted from the chilled water, causing the refrigerant to evapor
ate (turn into a vapor).
The refrigerant, now a cool, low-pressure vapor, absorbs heat from the c
hilled water, cooling it down.
This cooled water is then circulated to various areas for cooling, like air h
andling units (AHUs).
Chilling Plant Working
Compression:
Compression:
The low-pressure, low-temperature refrigerant vapor is then drawn into a comp
ressor.
The compressor increases the pressure and temperature of the refrigerant, tur
ning it into a high-pressure, high-temperature
Condensation:
The hot, high-pressure refrigerant vapor enters the condenser (another heat ex
changer).
The refrigerant releases its heat into the surrounding environment (air or cooli
ng tower water), causing it to condense back into a liquid state.
This heat rejection process is where the heat from the building is transferred o
ut.
Expansion:
The high-pressure, high-temperature liquid refrigerant then flows through an e
xpansion valve.
The expansion valve reduces the pressure and temperature of the refrigerant, p
reparing it for the next cycle.
The refrigerant then returns to the evaporator to start the process all over agai
n.
Chilling Plant SOP
START UP PROCESS :
Before starting the compressor, the utility operator checks & ensures following
: He ensures for the power availability.
: He ensures that the cooling tower circulation pump is ON & adequate pressure is sh
own on the pump.
: He ensures that the cooling tower fan is ON.
: He ensures that the chilling primary pump to chiller is ON & adequate pressure is
Shown on the pump.
: He will ensure that the level of NH3 in NH3 receiver is > 60%.
: He ensures that the level of the hot well tank is within limits.
: He will ensure that the oil level in the compressor is up to the 70%.
: Once all these parameters are checked & ensured, the utility operator starts the chilli
ng compressor.
Howden Blower & STPL Turbine
Preventive Maintenance:
Prepared by :
Vipendra Kumar
Howden Blower in Acid Plants
15
Importance of Howden Blower :-
●Howden blower is most significant and critical equipment of the acid plant.
●The blower compresses the gas to sufficient pressure to overcome the pressure
drop through the plant.
●In a sulphur burning acid plant, the gas handled by the blower is air. In a
regeneration or metallurgical acid plant the gas contains SO2
and traces of acid
mist.
●The gas must be dried in a Drying Tower before passing through the blower in
order to prevent corrosion from acid condensation.
Acid Blower
16
Blower Preventive Checklist :
17
Blower Silencer :
● Suction Silencer
opened found some
dust and cleaned by
air as well as
manually.
● Suction line flange
raise checked found
ok.
● wall thickness found
ok which is 6mm
18
Inlet guide vane valve : ( IGV )
19
Inlet guide vane valve : ( IGV )
20
Inlet guide vane valve : ( IGV )
21
Inspection and maintenance :
●Manual adjustment with handwheel and spindle and spindle found
free.
●Vane Bearing & Guide Roller
Lubricant quantity for relubrication: until grease comes out of the
lubrication point
●Hydraulic operated cylinder top up with the ISO VG - 32 ( 0.80ml)
All over IGV operated very smooth and free ,manually .
Blower Casing & Impeller :
● Casing window open
and check inside
casing visually
● welded Backward
curved blades
checked and there is
no wear &
corrosion
and
cr
ac
k.
● Rotor is Dynamically
balanced as per the
visually inspection as
well as not any rust
or
particle
found.
22
Bearing Housing :
● horizontally
split
casing checked,
split
housing inside found
o
k
● split housing inside
chamber
Cleaned by
air & cloth, surface of
split.there is
no
scoring or
marking
where insert bearing.
● Oil filling vent &
ventilation
filter
cleaned by
air.
23
Blower Bearing Clearance :
● Bearig
clearance - 0.03
mm(radially)the
re is no play or
inner & outer
race & Ball
found ok
24
Bearing Play :
1.Cylindrical Roller
Bearing NU 1026 M
● Grooved ball
bearing
Bearing 6222.C3
SKF
2. .Bearing
clearance - <
0.05 mm there is
no
play or inner &
outer
race & Ball found ok
25
Shaft :
● Shaft Condition no
wear and
Corrosion.
● Shaft checked
there is no scoring
and overheating or
not found any
heating spot.
26
Shaft Hub And Bearing Condition.
● The blower is
provided with
Double ball
bearing housing
and roller bearing
inserts.
● Lubrication by
oil bath.Oil grade
ISO VG 32.
● Hub condition and
bearing condition
found ok, as well
as there is no play
found.
27
Blower Coupling :
● Flexible couplings
between driver and
blower.
● torsionally elastic
and bending
elastic claw
coupling checked ,
Periphery cleaned
by air or cloth & no
damage or crack
on spider.
28
Clutch SSS :
The SSS clutch is
fitted between a
driving device and its
associated driven
machinery ( Motor &
Gearbox)
●Empty the existing
oil from the clutch by
removing the oil fill
hole to bottom dead
centre.
●Top up oil to top
dead centre & fill the
clutch with oil until it
flow from the oil level..
●Quantity of oil =
0.85lit. 29
Turbine Gearbox :
● Turbine gear
condition found ok
visually and gear
teeth has no wear
or corrosion.
30
Turbine Gearbox Gear :
● Turbine
gearbox
Axial play
checked
and it is - 0.015
31
Gearbox Backlash -
00
Gearbox Backlash -
0.018mm
Backlash :
32
Radially Play 00
mm
Radially Play 0.03
mm
Gearbox Radially :
33
Gearbox Housing :
● horizontally split
casing checked
visually , no wear
or corrosion and
there is scoring
or marking on
split where
bearing insert
found ok.
34
JOURNAL BEARINGS :
● Journal Bearing HS
Side
(Dri
ve
end)Journal
Bearings LS Side
(DriveEnd)
Drive
end
and non drive
end
both bearing
found
ok there is
no
marking
found
.
● Bearing clearance is
radially 0.02 mm
35
Overspeed trip
knob
Servo motor
valve
Turbine Controller:
36
Oil Filter :
● Cleaned the oil
filter by taking
out
and rinsing the
insert
gasoline
used for
Cleaning.
● New Oil
filter
replace
d
37
Turbine Shaft :
● Turbine shaft is
visually checked
and found ok and
runout is ok
Runout of shaft -
0.02 mm
38
Gear Pump ( Oil circulation)
● Pump body
surface is cleaned.
housing clearance
( 0.1mm)
● gear clearance is
ok ( < 0.06mm)
39
Condensate Pump : CEP
● Pump shaft replaced
cleaned
casing, impeller)
Coupling & spider
replaced.
● Water pump
strainner
cleaned by air
and water
40
Oil Cooler :
● Condenser tube
checked and clean
by SS wire brush
as well as by water
jet.
● Hydraulic taken
there is no
leakages in tube or
shell.
41
Oil Tank & Supply Unit :
● Oil tank condition
checked and
found ok
● Oil top up , ISO VG
46
● Oil supply unit
and pipe are
checked , pipe
fitted and leakage
connector
replaced with the
new.
42
Heat Rejection Equipment
Topic: Cooling Towers
Prepared by :
Vipendra Kumar
Cooling Towers
• Introduction
• Types of cooling towers Assessment of cooling towers
Energy efficiency opportunities
Introduction
• Main Features of Cooling Towers
Introduction
• Components of a cooling tower
• Frame and casing: support exterior enclosures
• Fill: facilitate heat transfer by maximizing water / air contact
• Splash fill
• Film fill
• Cold water basin: receives water at bottom of tower
Introduction
• Components of a cooling tower
• Drift eliminators: capture droplets in air stream
• Air inlet: entry point of air
• Louvers: equalize air flow into the fill and retain water
within tower
• Nozzles: spray water to wet the fill
• Fans: deliver air flow in the tower
Types of Cooling Towers
• Natural Draft Cooling Towers
• Hot air moves through tower
• Fresh cool air is drawn into the tower from bottom
• No fan required
• Concrete tower <200 m
• Used for large heat duties
Types of Cooling Towers
• Natural Draft Cooling Tower
Types of Cooling Towers
• Mechanical Draft Cooling Towers
Large fans to force air through circulated water.
Water falls over fill surfaces: maximum heat transfer.
Cooling rates depend on many parameters
Can be grouped, e.g. 8-cell tower
Types of Cooling Towers
• Mechanical Draft Cooling Towers
Three types
 Forced draft
 Induced draft cross flow
 Induced draft counter flow
Types of Cooling Towers
• Forced Draft Cooling Towers
Air blown through tower by centrifugal fan at air inlet
Advantages: suited for high air resistance & fans are relatively quiet
Disadvantages: recirculation due to high air-entry and low air-exit
velocities
Types of Cooling Towers
• Induced Draft Cooling Towers
Two types
Cross flow
Counter flow
Advantage: less recirculation than forced draft towers
Disadvantage: fans and motor drive mechanism
require weather-proofinh
Types of Cooling Towers
Induced Draft Counter Flow CT
•Hot water enters at the top
•Air enters at bottom and exits at top
•Uses forced and induced draft fans
Types of Cooling Towers
• Water enters top and passes over fill
• Air enters on one side or opposite sides
• Induced draft fan draws air across fill
Induced Draft Cross Flow CT
Assessment of Cooling Towers
Measured Parameters
•Wet bulb temperature of air
•Dry bulb temperature of air
•Cooling tower inlet water temperature
•Cooling tower outlet water temperature
•Exhaust air temperature
•Electrical readings of pump and fan motors
•Water flow rate
•Air flow rate
Assessment of Cooling Towers
Performance Parameters
1. Range
1.Approach
2.Effectiveness
3.Cooling capacity
4.Evaporation loss
5.Cycles of concentration
6.Blow down losses
•Liquid / Gas ratio
Assessment of Cooling Towers
1. Range
Range (°C) = CW inlet temp
– CW outlet temp
High range = good
performance
Assessment of Cooling Towers
• 2. Approach
• Difference between cooling tower outlet cold water
temperature and ambient wet bulb temperature:
Approach (°C) =
CW outlet temp – Wet bulb temp
Assessment of Cooling Towers
4. Cooling Capacity
Heat rejected in kCal/hr or tons of refrigeration (TR)
= mass flow rate of water X specific heat X temperature
difference
High cooling capacity = good performance
Assessment of Cooling Towers
5. Evaporation Loss
Water quantity (m3/hr) evaporated for cooling duty
= theoretically, 1.8 m3 for every 10,000,000 kCal heat rejected
= 0.00085 x 1.8 x circulation rate (m3/hr) x (T1-T2)
T1-T2 = Temp. difference between inlet and outlet water
Assessment of Cooling Towers
Cycles of concentration (C.O.C.)
Depend on cycles of concentration and the evaporation losses
Blow Down =
Evaporation Loss / (C.O.C. – 1)
Assessment of Cooling Towers
Liquid Gas (L/G) Ratio
Ratio between water and air mass flow rates
Heat removed from the water must be equal to the heat absorbed by
the surrounding air
L(T1 – T2) = G(h2 – h1)
L/G = (h2 – h1) / (T1 – T2)
T1 = hot water temp (oC) T2 = cold water temp (oC)
Enthalpy of air water vapor mixture at inlet wet bulb temp (h1)
and outlet wet bulb temp (h2)
Energy Efficiency Opportunities
1. Selecting a cooling tower
2. Fills
3. Pumps and water distribution
4. Fans and motors
Energy Efficiency Opportunities
1. Selecting a cooling tower
Range
Range
Range determined by process, not by system
Approach
Closer to the wet bulb temperature
Bigger size cooling tower
More expensive
CT NAME
DESCRIPTIO
N
6MW CT 2.35 MW CT SO3 OT-1
Model No.
------ PFC -25516 ------ PFC - 24414 -------
Make ----- CANARA BlueChip Canara Canara
Type of Flow
Cross /
Counter
CROSS Counter Counter Cross
Design I/L T Deg C 42 37 37 37
O/L T Deg C 32 32 32 32
WBT Deg C 28 28 28 28
Capacity Flow M3/HR 1500 200 700 400
Capacity TR 4960 331 1157 661
Chapter 3 : Water Treatment Plant
(Zero Lequid Dischrge)
Zero Liquid Dischrge
: Zero liquid discharge (ZLD) refers to a treatment process in
which the plant discharges no liquid effluent into surface
waters, in effect completely eliminating the environmental
pollution associated with treatment.
: In Aarti Industry zld system are given bellow,
: MEE Plant ( Multi effect evoporative plant)
: ATFD ( Agitator thin filter dryer )
: ETP ( Effuilent treatment plant)
Zld section
• MEE plant Cappicity : 80 KLD
• Process : Waste water
treatment Plant
• Feed water parameter : 25000
TDS , PH - 7 ppm
• Condenstate water parameter
: 800 TDS , PH - 7 ppm
• Consentrate water
paremeter : 100000 TDS
• Steam inlet pressure :
2 kg/cm2
• Vacuum required : 710 mmhg
before and after steam supply
680 mmhg
ATFD
• After MEE Plant waste water feed in ATFD for slurries waste
water convert to dry powder form by steam and rotataing
equipment.
• Key Components of ATFD
• Feed System: Introduces the liquid, slurry, or paste to the dryi
ng process.
• Rotating Shaft with Blades or Wipers: Agitates the material, e
nsuring it forms a thin, even film on the heated surface.
• Heated Surface (Jacketed Cylinder): Provides the necessary h
eat for evaporation.
• Vapor Outlet: Removes the evaporated moisture or solvent.
• Discharge System: Collects the dried product.
ATFD
Outcomes
• Through my 90 day internship , I have learnt how to handle
with real work time conditions.
• Also how maintaining relations with your seniors and
batchmates help you grow into your job.They can guide you
whenever you are stuck at situations.
• It helped me gain insights on to day to day oprations and
maintenance.
• I got traditional working culture and eniornment.
• My guide helped me how to apply theoretical knowledge to
pratical knowledge.
CONCLUSION
• The Summer Internship was more than learning experience
for me. I got learnt about real work time conditions and learnt
them. Learnt about how to handle pressure and how
maintaining relations with collegues and seniors is important
in your job.
• The overall experience was fun and learing in many ways.
Thank
you
41

S internship eight semester prersentation

  • 1.
    Gujrat Technical university LaxmiInstute of Technology Sarigam Valsad Prepared By Vipendra Kumar 220863119015
  • 2.
    CONTENTS • Internship Details •Objectives • Introduction • • Brief About Aarti Industry • Production Range • Utility Maintenance • Water treatment plant • Outcomes • Conclusions
  • 3.
    Objectives Technical Objectives : 1.Gain improvement in SAP system. 2 . Learn industry-based standard practices like kaizen and 5S" activity. Soft Skill Objectives: 1 . Improving communication and presentation skills. 2. Learn problem solving and thunking abilities. Personal Growth Objectives : 1 . Contribute to the compnay and its goals. 2 . Gain valuable industry experience and build a professional work. 3 . Gain Knowledge industry working culture and gain experience equipments.
  • 4.
    Internship Details • CompanyName - Aarti Industries LTD Vapi • External Guide - Sudhir Gupta • Internal Guide - Hemant Patel • Department - Utility Maintenance / Engg. Department • Role : intern/ Trainee • Location: Vapi • From : 19/03/2025 to 19/04/2025 • Working Hour : 09:00 AM To 17:30 PM
  • 5.
    Chapter 1 :Introduction
  • 6.
    Introduction Acid Division AppleDevision Fertilizer Organic Devi sion Necent Division Amine De vis ion
  • 7.
    Different Chemical UnderAarti Industry SULFURIC ACID LIQUID SO3 DI-METHYLE SULPHATE PNCB CSA OLEUM DCB GYPSUM DCP NITRO BENZENE HYDROCHLORIC ACID NITRIC ACID
  • 8.
    Chapter 2 :Utility Maintenance (Chilling Plant)
  • 9.
    Introduction of Chillingplant Chiiling Plant Cappicity : 60 TR Refrigrerant Name : 134A COMPRESSOR TYPE : Dual srew compressor Condensor Type : Water shell and tube type Condensor Evoporator Type : Shell and Tube type Hot and Cold Well : 30 M2 Area Insulation type : Nitraile type cold insulation ( thick ness - 50 mm) Insulation Density : 60 mm Chilling water outlet Temp. : 7 deree celcius Chilling water inlet Temp. : 12 degree celceus Cooling tower cappicity : 100 TR Primary circulation pump : 35 m3/hr Secondary circulation pump : 35 m3/hr
  • 10.
  • 11.
    Chiiling plant working Chillerplant works by using a refrigeration cycle to transfer heat from a sou rce (like chilled water) to a heat sink (like cooling tower or air). This proc ess involves a refrigerant that undergoes phase changes (liquid to vapor and back), absorbing and releasing heat along the way. Chilling plant Main Four Components are bellow ; 1. Evaporation: Liquid refrigerant enters the evaporator (a heat exchanger). Heat is extracted from the chilled water, causing the refrigerant to evapor ate (turn into a vapor). The refrigerant, now a cool, low-pressure vapor, absorbs heat from the c hilled water, cooling it down. This cooled water is then circulated to various areas for cooling, like air h andling units (AHUs).
  • 12.
    Chilling Plant Working Compression: Compression: Thelow-pressure, low-temperature refrigerant vapor is then drawn into a comp ressor. The compressor increases the pressure and temperature of the refrigerant, tur ning it into a high-pressure, high-temperature Condensation: The hot, high-pressure refrigerant vapor enters the condenser (another heat ex changer). The refrigerant releases its heat into the surrounding environment (air or cooli ng tower water), causing it to condense back into a liquid state. This heat rejection process is where the heat from the building is transferred o ut. Expansion: The high-pressure, high-temperature liquid refrigerant then flows through an e xpansion valve. The expansion valve reduces the pressure and temperature of the refrigerant, p reparing it for the next cycle. The refrigerant then returns to the evaporator to start the process all over agai n.
  • 13.
    Chilling Plant SOP STARTUP PROCESS : Before starting the compressor, the utility operator checks & ensures following : He ensures for the power availability. : He ensures that the cooling tower circulation pump is ON & adequate pressure is sh own on the pump. : He ensures that the cooling tower fan is ON. : He ensures that the chilling primary pump to chiller is ON & adequate pressure is Shown on the pump. : He will ensure that the level of NH3 in NH3 receiver is > 60%. : He ensures that the level of the hot well tank is within limits. : He will ensure that the oil level in the compressor is up to the 70%. : Once all these parameters are checked & ensured, the utility operator starts the chilli ng compressor.
  • 14.
    Howden Blower &STPL Turbine Preventive Maintenance: Prepared by : Vipendra Kumar
  • 15.
    Howden Blower inAcid Plants 15 Importance of Howden Blower :- ●Howden blower is most significant and critical equipment of the acid plant. ●The blower compresses the gas to sufficient pressure to overcome the pressure drop through the plant. ●In a sulphur burning acid plant, the gas handled by the blower is air. In a regeneration or metallurgical acid plant the gas contains SO2 and traces of acid mist. ●The gas must be dried in a Drying Tower before passing through the blower in order to prevent corrosion from acid condensation.
  • 16.
  • 17.
  • 18.
    Blower Silencer : ●Suction Silencer opened found some dust and cleaned by air as well as manually. ● Suction line flange raise checked found ok. ● wall thickness found ok which is 6mm 18
  • 19.
    Inlet guide vanevalve : ( IGV ) 19
  • 20.
    Inlet guide vanevalve : ( IGV ) 20
  • 21.
    Inlet guide vanevalve : ( IGV ) 21 Inspection and maintenance : ●Manual adjustment with handwheel and spindle and spindle found free. ●Vane Bearing & Guide Roller Lubricant quantity for relubrication: until grease comes out of the lubrication point ●Hydraulic operated cylinder top up with the ISO VG - 32 ( 0.80ml) All over IGV operated very smooth and free ,manually .
  • 22.
    Blower Casing &Impeller : ● Casing window open and check inside casing visually ● welded Backward curved blades checked and there is no wear & corrosion and cr ac k. ● Rotor is Dynamically balanced as per the visually inspection as well as not any rust or particle found. 22
  • 23.
    Bearing Housing : ●horizontally split casing checked, split housing inside found o k ● split housing inside chamber Cleaned by air & cloth, surface of split.there is no scoring or marking where insert bearing. ● Oil filling vent & ventilation filter cleaned by air. 23
  • 24.
    Blower Bearing Clearance: ● Bearig clearance - 0.03 mm(radially)the re is no play or inner & outer race & Ball found ok 24
  • 25.
    Bearing Play : 1.CylindricalRoller Bearing NU 1026 M ● Grooved ball bearing Bearing 6222.C3 SKF 2. .Bearing clearance - < 0.05 mm there is no play or inner & outer race & Ball found ok 25
  • 26.
    Shaft : ● ShaftCondition no wear and Corrosion. ● Shaft checked there is no scoring and overheating or not found any heating spot. 26
  • 27.
    Shaft Hub AndBearing Condition. ● The blower is provided with Double ball bearing housing and roller bearing inserts. ● Lubrication by oil bath.Oil grade ISO VG 32. ● Hub condition and bearing condition found ok, as well as there is no play found. 27
  • 28.
    Blower Coupling : ●Flexible couplings between driver and blower. ● torsionally elastic and bending elastic claw coupling checked , Periphery cleaned by air or cloth & no damage or crack on spider. 28
  • 29.
    Clutch SSS : TheSSS clutch is fitted between a driving device and its associated driven machinery ( Motor & Gearbox) ●Empty the existing oil from the clutch by removing the oil fill hole to bottom dead centre. ●Top up oil to top dead centre & fill the clutch with oil until it flow from the oil level.. ●Quantity of oil = 0.85lit. 29
  • 30.
    Turbine Gearbox : ●Turbine gear condition found ok visually and gear teeth has no wear or corrosion. 30
  • 31.
    Turbine Gearbox Gear: ● Turbine gearbox Axial play checked and it is - 0.015 31
  • 32.
    Gearbox Backlash - 00 GearboxBacklash - 0.018mm Backlash : 32
  • 33.
    Radially Play 00 mm RadiallyPlay 0.03 mm Gearbox Radially : 33
  • 34.
    Gearbox Housing : ●horizontally split casing checked visually , no wear or corrosion and there is scoring or marking on split where bearing insert found ok. 34
  • 35.
    JOURNAL BEARINGS : ●Journal Bearing HS Side (Dri ve end)Journal Bearings LS Side (DriveEnd) Drive end and non drive end both bearing found ok there is no marking found . ● Bearing clearance is radially 0.02 mm 35
  • 36.
  • 37.
    Oil Filter : ●Cleaned the oil filter by taking out and rinsing the insert gasoline used for Cleaning. ● New Oil filter replace d 37
  • 38.
    Turbine Shaft : ●Turbine shaft is visually checked and found ok and runout is ok Runout of shaft - 0.02 mm 38
  • 39.
    Gear Pump (Oil circulation) ● Pump body surface is cleaned. housing clearance ( 0.1mm) ● gear clearance is ok ( < 0.06mm) 39
  • 40.
    Condensate Pump :CEP ● Pump shaft replaced cleaned casing, impeller) Coupling & spider replaced. ● Water pump strainner cleaned by air and water 40
  • 41.
    Oil Cooler : ●Condenser tube checked and clean by SS wire brush as well as by water jet. ● Hydraulic taken there is no leakages in tube or shell. 41
  • 42.
    Oil Tank &Supply Unit : ● Oil tank condition checked and found ok ● Oil top up , ISO VG 46 ● Oil supply unit and pipe are checked , pipe fitted and leakage connector replaced with the new. 42
  • 43.
    Heat Rejection Equipment Topic:Cooling Towers Prepared by : Vipendra Kumar
  • 44.
    Cooling Towers • Introduction •Types of cooling towers Assessment of cooling towers Energy efficiency opportunities
  • 45.
  • 46.
    Introduction • Components ofa cooling tower • Frame and casing: support exterior enclosures • Fill: facilitate heat transfer by maximizing water / air contact • Splash fill • Film fill • Cold water basin: receives water at bottom of tower
  • 47.
    Introduction • Components ofa cooling tower • Drift eliminators: capture droplets in air stream • Air inlet: entry point of air • Louvers: equalize air flow into the fill and retain water within tower • Nozzles: spray water to wet the fill • Fans: deliver air flow in the tower
  • 48.
    Types of CoolingTowers • Natural Draft Cooling Towers • Hot air moves through tower • Fresh cool air is drawn into the tower from bottom • No fan required • Concrete tower <200 m • Used for large heat duties
  • 49.
    Types of CoolingTowers • Natural Draft Cooling Tower
  • 50.
    Types of CoolingTowers • Mechanical Draft Cooling Towers Large fans to force air through circulated water. Water falls over fill surfaces: maximum heat transfer. Cooling rates depend on many parameters Can be grouped, e.g. 8-cell tower
  • 51.
    Types of CoolingTowers • Mechanical Draft Cooling Towers Three types  Forced draft  Induced draft cross flow  Induced draft counter flow
  • 52.
    Types of CoolingTowers • Forced Draft Cooling Towers Air blown through tower by centrifugal fan at air inlet Advantages: suited for high air resistance & fans are relatively quiet Disadvantages: recirculation due to high air-entry and low air-exit velocities
  • 53.
    Types of CoolingTowers • Induced Draft Cooling Towers Two types Cross flow Counter flow Advantage: less recirculation than forced draft towers Disadvantage: fans and motor drive mechanism require weather-proofinh
  • 54.
    Types of CoolingTowers Induced Draft Counter Flow CT •Hot water enters at the top •Air enters at bottom and exits at top •Uses forced and induced draft fans
  • 55.
    Types of CoolingTowers • Water enters top and passes over fill • Air enters on one side or opposite sides • Induced draft fan draws air across fill Induced Draft Cross Flow CT
  • 56.
    Assessment of CoolingTowers Measured Parameters •Wet bulb temperature of air •Dry bulb temperature of air •Cooling tower inlet water temperature •Cooling tower outlet water temperature •Exhaust air temperature •Electrical readings of pump and fan motors •Water flow rate •Air flow rate
  • 57.
    Assessment of CoolingTowers Performance Parameters 1. Range 1.Approach 2.Effectiveness 3.Cooling capacity 4.Evaporation loss 5.Cycles of concentration 6.Blow down losses •Liquid / Gas ratio
  • 58.
    Assessment of CoolingTowers 1. Range Range (°C) = CW inlet temp – CW outlet temp High range = good performance
  • 59.
    Assessment of CoolingTowers • 2. Approach • Difference between cooling tower outlet cold water temperature and ambient wet bulb temperature: Approach (°C) = CW outlet temp – Wet bulb temp
  • 60.
    Assessment of CoolingTowers 4. Cooling Capacity Heat rejected in kCal/hr or tons of refrigeration (TR) = mass flow rate of water X specific heat X temperature difference High cooling capacity = good performance
  • 61.
    Assessment of CoolingTowers 5. Evaporation Loss Water quantity (m3/hr) evaporated for cooling duty = theoretically, 1.8 m3 for every 10,000,000 kCal heat rejected = 0.00085 x 1.8 x circulation rate (m3/hr) x (T1-T2) T1-T2 = Temp. difference between inlet and outlet water
  • 62.
    Assessment of CoolingTowers Cycles of concentration (C.O.C.) Depend on cycles of concentration and the evaporation losses Blow Down = Evaporation Loss / (C.O.C. – 1)
  • 63.
    Assessment of CoolingTowers Liquid Gas (L/G) Ratio Ratio between water and air mass flow rates Heat removed from the water must be equal to the heat absorbed by the surrounding air L(T1 – T2) = G(h2 – h1) L/G = (h2 – h1) / (T1 – T2) T1 = hot water temp (oC) T2 = cold water temp (oC) Enthalpy of air water vapor mixture at inlet wet bulb temp (h1) and outlet wet bulb temp (h2)
  • 64.
    Energy Efficiency Opportunities 1.Selecting a cooling tower 2. Fills 3. Pumps and water distribution 4. Fans and motors
  • 65.
    Energy Efficiency Opportunities 1.Selecting a cooling tower Range Range Range determined by process, not by system Approach Closer to the wet bulb temperature Bigger size cooling tower More expensive
  • 66.
    CT NAME DESCRIPTIO N 6MW CT2.35 MW CT SO3 OT-1 Model No. ------ PFC -25516 ------ PFC - 24414 ------- Make ----- CANARA BlueChip Canara Canara Type of Flow Cross / Counter CROSS Counter Counter Cross Design I/L T Deg C 42 37 37 37 O/L T Deg C 32 32 32 32 WBT Deg C 28 28 28 28 Capacity Flow M3/HR 1500 200 700 400 Capacity TR 4960 331 1157 661
  • 67.
    Chapter 3 :Water Treatment Plant (Zero Lequid Dischrge)
  • 68.
    Zero Liquid Dischrge :Zero liquid discharge (ZLD) refers to a treatment process in which the plant discharges no liquid effluent into surface waters, in effect completely eliminating the environmental pollution associated with treatment. : In Aarti Industry zld system are given bellow, : MEE Plant ( Multi effect evoporative plant) : ATFD ( Agitator thin filter dryer ) : ETP ( Effuilent treatment plant)
  • 69.
    Zld section • MEEplant Cappicity : 80 KLD • Process : Waste water treatment Plant • Feed water parameter : 25000 TDS , PH - 7 ppm • Condenstate water parameter : 800 TDS , PH - 7 ppm • Consentrate water paremeter : 100000 TDS • Steam inlet pressure : 2 kg/cm2 • Vacuum required : 710 mmhg before and after steam supply 680 mmhg
  • 70.
    ATFD • After MEEPlant waste water feed in ATFD for slurries waste water convert to dry powder form by steam and rotataing equipment. • Key Components of ATFD • Feed System: Introduces the liquid, slurry, or paste to the dryi ng process. • Rotating Shaft with Blades or Wipers: Agitates the material, e nsuring it forms a thin, even film on the heated surface. • Heated Surface (Jacketed Cylinder): Provides the necessary h eat for evaporation. • Vapor Outlet: Removes the evaporated moisture or solvent. • Discharge System: Collects the dried product.
  • 71.
  • 72.
    Outcomes • Through my90 day internship , I have learnt how to handle with real work time conditions. • Also how maintaining relations with your seniors and batchmates help you grow into your job.They can guide you whenever you are stuck at situations. • It helped me gain insights on to day to day oprations and maintenance. • I got traditional working culture and eniornment. • My guide helped me how to apply theoretical knowledge to pratical knowledge.
  • 73.
    CONCLUSION • The SummerInternship was more than learning experience for me. I got learnt about real work time conditions and learnt them. Learnt about how to handle pressure and how maintaining relations with collegues and seniors is important in your job. • The overall experience was fun and learing in many ways.
  • 74.