Post on 27-Nov-2014
Superefficient Four Pass Fire Tube Steam BoilersSTEAMSTAR
Hi h Th l Effi i f 95%High Thermal Efficiency of 95%on NCVFull wet back design.Economizer as heat recoveryunit.Full protection against cold endp gcorrosion.Fully automatic operation.Continuous modulation Burners.Robust dependable flamemonitoring system.Easy for maintenance.Self cleaning flue gas velocitiesfor high operating efficiency.Reliable robust steam heavy fueloil heating pumping units.No fuel oil ring mains neededNo fuel oil ring mains needed.Gravity supply sufficient.Third party inspection availableinternationally acceptable.
Transparent Energy Systems Pvt. Ltd.Pune- 37. (INDIA)Tel : 020 – 24211347, Fax : 020 – 24212533. E-mail : trans@pn2.vsnl.net.in projectsales@tespl.comWebsite : www.tespl.com
Technical Specification
Sr. No. Parameter Unit Description1 Model STEAMSTAR
2 Type Horizontal, Full Wet Back, Smoke TubeType, With Economizer & Steam heatedhot water Generator (* Optional add-onAccessories for Higher Efficiency)
3 Rated Steam Output (F& a-100 Deg.C) Kg/hr 1000 to 14000
Steam Pressure in Boiler Kg / cm2 (g) 7 to 10 (Adjustable)
Safety Valve Set Pressure Kg / cm2 (g) 10.5
Design Code ASME / BS 2790 / IBR, 1996 with Latest Ammendments
Steam Condition Dry & Saturated
Dryness Fraction 0.98 (Minimum)
4
5
6
7
8 y 0.98 (Minimum)
No. of Flue Gas Passes3 passes in Boiler4 th in economizer
Fuel Suitability Furnace oil / LDO / HSD
Thermal Efficiency (based on NCV)
With Economiser & Steam Heated H.W.G % 95 ± 1
9
10
11
a)
Only Boiler % 89 ± 1
Steam to Fuel Ratio : (On Furnace oil havingNCV of 9710 Kcal/kg)
Kg / Kg (F & A 100 Deg.C) (From F. W-at 90 Deg.C and Steam
at 10.54 Kg/ Cm2.g)
& S G 17 08 16 07
b)
12
a) With Economizer & Steam heated H.W.G. 17.08
16.00
16.07
15.05Only Boiler
Tolerance on Steam to Fuel ratio % ±1
Electric Supply AC 3 Phase with Neutral (4 Wire)
a)
b)
13
14 Electric Supply AC 3 Phase with Neutral (4 Wire)
Type of Burner Modulation High Low Modulation , Stepless
Notes :
14
15
1) The Client should supply the Fuel oil as per –IS-1593-1988 & Feed Water to boiler as per IS-10392-1982 at the required Pressure and Temperature specified in the Input – Output specification sheet.
2) To obtain fuel consumption of particular model, multiply the steam output (f & a 100 Deg.C) by steamto fuel ratio ( f & a 100 Deg.C)
Input & Output SpecificationINPUT
A] FEED WATER AT THE INLET OF THE FEED PUMP SUCTIONQuality As per IS – 10392 – 1982
Temperature
Pressure at the pumpsuction
Deg.C
Kg/cm2(g)
90 to 110
0.3 to 2.0
BOILER WATER SPECIFICATION IN THE BOILER DRUMB]Quality
TDS
As per IS-10392-1982
3200 - 3500
FUEL OIL AT THE INLET OF THE SUCTION FILTER OF THE HEATING PUMPING UNITC]
TYPE
Quality
TemperaturePressure at the Suction Filter (Min)
Deg.C
Kg/Cm2(g)
Furnace Oil
As per IS-1593
70 to 90
0.3 to 2.0
LDO / HSD
As per IS-1460-1995
20 to 70
0.3 to 2.0( )
INSTRUMENT AIR AT INLET OF THE RESPECTIVE INSTRUMENTSTYPE Compressed air
QualityTemperaturePressureDew Point
Deg.CKg/cm2(g)
Deg.C
As per BS-6739-1986 or ANSI/ASA-57.3-197510 to 504.5 to 5.5
At least 10 Deg.C below lowest ambient temp.
D]
DustOil Content
g At least 10 Deg.C below lowest ambient temp.Filtered below 3-5 micron
Not to exceed 1 ppm
E] ELECTRICAL SUPPLY AT CONTROL PANEL INCOMERTYPEQualityVoltage
3-PHASE AC (with Neutral) 4 WireAs per IS-12360-1988
415V+/-6%
OUTPUTFrequency 50Hz+/-3%
A] STEAM AT THE OUTLET OF STEAM SHOP VALVEDryness Fraction * Dryness fraction 0.98 or Higher at Normal Water Level
Moisture in SteamComposition of MoisturePressure at the Outlet ***
% ≤2Same as Boiler Water
B] FLUE GAS AT FLUE GAS OUTLET (IN CLEAN BOILER CONDITIONS)LDO / HSD FO
1 Smoke spot No.(As per ASTM D2156-63T) Less Than 2 Less Than 3
Suspended Particulate 2 PPM LDO = 537 multiplied by ACHSD 524 multiplied by AC FO = 562 multiplied by AC
Kg/Cm2(g)Same as Boiler Water
7 to 9.9
pMatter (Approximate) HSD = 524 multiplied by AC FO 562 multiplied by AC
It is the responsibility of buyer / user to verify & ensure that the flue gas specifications mentioned above meet the statutory pollution norms stipulated and areaccepted by concerned authorities. In case the above specifications do not meet the requirements buyer / user is requested to contact Transparent so that a suitablepollution abatement equipment to meet the requirements is offered at a additional cost.*- Dryness Fractions subject to maintaining minimum steam Pressure & Normal Boiler water level in the Steam Drum**- Output guaranteed are subject to input conditions been met as specified above***- Steam pressure is adjustable. The Boiler will maintain set pressure provided the steam demand does not exceed rated capacity.
Where AC is Ash Content in fuel expressed in %
Superior Features
FEATURES
1. System gives 95% efficiency even with condensate return at 125oC.
2. 95% efficiency is minimum achievable irrespective of the fuel used and is typical for
furnace oil with 4.5% sulphur content. For low sulphur content fuel it can be improved
to 96.5%
3. Single stage economizer with finned tube construction makes the heat recovery unit
very compact. This reduces the surface area of the equipment and related losses.
4. Single stage economizer offers very low-pressure drop in comparison with air
preheater and hence reduces the fan power requirement and operating costs.
5. Steam heated water preheater maintains the water inlet temperature to economizer
above 125oC. This maintains the heating surfaces of economizer always above 125oC
to eliminate cold end corrosion possibilities.
6. Simple and robust control circuit reduces the initial cost and ensures high reliability ofthe system. Cold end corrosion is prevented even in part load conditions.
7. Automatic flue gas diverter valve is incorporated in the system to divert the flue gas tog p y g
chimney bypassing economizer during cold start conditions until water temperature at
economizer inlet reaches 125oC.
8. Condensate from steam-heated water preheater can be put back into feed water tankconserving energy and water.
9 Requirement of high temperature withstanding burner components is eliminated in9. Requirement of high temperature withstanding burner components is eliminated in
contrast with air preheater.
10. Less ducting work is required for economizer in comparison with air preheater which
reduces the initial cost.
11. Heat recovery and efficiency is not affected for fluctuating or part load conditions
12. Entire system can be dispatched as single unit depending on the capacity and size.
Even if they are sent as separate components, its is mechano type assembly minimizing
site work.
13. Economizer surfaces are easily accessible for cleaning on flue gas side.
14. Presence of flue gas diverter valve enables cleaning and maintenance of economizerwith out stopping the boiler.
Comparative Statement
Comparative Statement of Transparent Make Steamstar V/s Other Make Boilers
TRANSPARENT (STEAMSTAR) OTHER MAKE BOILER
A] Efficiency :
High Thermal Efficiency of 95% on NCV of Fuel
Economizer with steam heated hot water generatoras Heat Recovery Unit on Standard models.
Thermal Efficiency of 88% on NCV of Fuel
No standard Heat Recovery Unit
1)
2)
B] Superior Thermal Design :
Four long passes of flue gases resulting inlarge residence time and effective heattransfer.
Standard 3 pass design
4th pass
3rd pass2nd pass 3rd pass
2nd pass
3)
Economiser
1st pass
3 pass
1st pass
CC] High sinking time
Water Starvation
Location of the furnace is at the bottom mostpoint in the shell. The water content above thetop upto normal working level is huge. This
Eccentric Furnace type Boiler has low sinking time.
The Furnace being located at one side at ati l l l i th h ll V ll
g gfeature provides very high sinking time. Furnacebeing subjected to very high temp flame is themost sensitive part of Boiler and needs to bealways covered by water. If the pump fails tosupply necessary quantity of water when theboiler is firing at full load. The water level goesbelow the NWL. If the safeties do not trip theburner water level will further drop and at one
comparatively upper level in the shell. Very smallwater content between furnace top and NWLresults in very short sinking time less than 8-10minutes. Operator does not get sufficient time tosave the furnace collapse in abnormal conditions.
point the the furnace top will be dry time requiredfor water level to go down from NWL to furnacetop is called as sinking time. In TES Boilers thesinking time as high as 45 Minutes. This providessufficient time for operator to save the boiler fromFurnace collapse in abnormal condition.
Comparative Statement
Comparative Statement of Transparent Make Steamstar V/s Other Make Boilers
TRANSPARENT (STEAMSTAR) OTHER MAKE BOILER
D] Symmetrical water circulation :
Centrally located Furnace ensures SymmetricalWater circulation hence uniform temperatureprofile.
Eccentric furnace does not have symmetric watercirculation hence leads to water starvation near theFurnace.
1)
Plain Cylindrical furnaces ensures stream linedair flow pattern which gives steady flamegeometry and are easy to clean and maintain.They are reasonable in cost and easy to Repair.
Due to corrugations in the furnace air flow ishighly Fluctuating and changing. This causesFlame impingement and cleaning is difficult. Theyare costly and difficult to repair.
Optimized configuration of Heating surfaces andTube size ensures adequate flue gas conveyingvelocities inside the tubes. This minimizesdeposition of particulate matter on the tubes
Large tube sizes lowers conveying Velocities andparticulate deposition is more resulting in frequentCleaning Frequency and are costly and verydifficult to repair
E] Heating and Pumping Unit :
deposition of particulate matter on the tubesthere by reducing Cleaning Frequency.
difficult to repair.
High Boiler availability for production due to less maintenance and Easy Maintenance
Fuel pump fitted with mechanical seal for200oC. Temp. application.
This feature is not given in all boilers
Specially designed of Filters on suction (2Nos– 1W+1S) This Filters are designed for Fullfloweven at 80% clogging with help of largefilters area. Full bore ball valves of inlet pipesize eliminates any possibility of flowrestriction. This increases pump life. There isno need of ring main. Suction to pump byGravity is sufficient
The CI duplex filters design demands frequentcleaning. These filters have less filtering area andvery small opening of integral ball valves whichrestrict the flow of resulting in shorter life of pumps.In case of Fuel pumping ring main isrecommended which causes a additional powerResulting in additional running cost.
Gravity is sufficient.
Comprehensive solid carbon steel piping isprovided to Fuel Oil Heater for series, parallel &bypass operation. This helps maintenance ofthe steam/electric heater while boiler isoperational. In our case the piping is done insuch a way that you can use the heater in fourmodes Only steam heating isolating Electrical
This facility is not provided.
modes. Only steam heating isolating Electricalheater . Only Electrical heating isolating (50%load) Steamheater. Both the heaters in series incase of Emergency. Bypass both in case of lightoil firing.
Comparative Statement
Comparative Statement of Transparent Make Steamstar V/s Other Make Boilers
TRANSPARENT (STEAMSTAR) OTHER MAKE BOILER
Separate steam & electric heater ensures thateither of the two can be attended to withoutshutdown of Boiler. You can replace electricheater without stopping the boiler or do anymaintenance on steam heater.
Common Steam Cum Electric Heater hence theyhave to be attended by stopping the boiler.
Pressure gauges at fuel pump & water pump No gauges are provided for filter cloggingsuction to identify filter Blockage & pump suctionconditions.
indication hence results in pump starvation.
Pressure Gauge (-1.0 to 0.6 kg/Cm2.) for fuelpump & Feed Pump suction to detect vapor lockcaviation in suction line and filter cleaningneeds.
Digital temp controller maintains constant
No provision is made to take care of vapor lock.
Thermostat & dial type controller has tolerance ofg paccurate temp.
Thermostat & dial type controller has tolerance of+-5oC which results in varation in viscosity andpoor atomization leading to adverse effects oncombustion of fuel.
Isolation Ball Valve at inlet & outlet of Oil SuctionFilter for cleaning of filter without shutdown ofequipment.
Duplex filter with common handle provided whichprefers ring main system due to insufficient flowareas.
S i ll d i d i & f l t ithSpecially designed air & fuel separator withpressure indicator to eliminate airlock & troublefree performance of fuel pump.
Airlocking Tendency is high as this provision is notmade.
Highly reliable Steam Control valve on steamHeater
Solenoid valve is provided which has tendency toleak
Burner Firing Sequence Controller is highlyreliable own make made from standard
Electronic sequence controller is provided which isl li bl d i hi h ireliable own make made from standard
high quality switchgear viz –a) Timer of Cutler Hammer.b) Relays of OEN or Pla, 230V AC, 10 amo.
Rating.c) High Wattage Photocell imported from
Japan.d) Epoxy Cast Environment-proof Electronic
Circuit possibility of solder or cable stand
less reliable and expensive which requirescomplete replacement in case of and problem
Photocell is delicate and less reliable.
Circuit possibility of solder or cable standbreakage.
Control Panel
Powder Coated Panel
• Control Circuit Wiring with solid conductorsingle strand with ferrule number.
• Resistance backed long life indicating bulbs
Painted panel
• Stranded cable loose wiring is done. Tracingof the wiring is difficult.
Resistance backed long life indicating bulbs.• HRC Fuses for all Motors & O/L protection
& single phasing prevention.• MCB as Control Fuse.• Solid Conductor Cable Wring to eliminate
loose Contact possibility.
• Not Provided• Loose contact possibility is high
Comparative Statement
Comparative Statement of Transparent Make Steamstar V/s Other Make Boilers
TRANSPARENT (STEAMSTAR) OTHER MAKE BOILER
Tube Overheat Control And Water Level Safeties
Tube overheat Temperature Controller Sensordetects the temperature of flue gases flowing in3rd pass tubes upper row. It trips firing even ifBWLC fails to detect no water level Further
Tube over heat controller not provided lesspossibility of damage to the boiler in case ofMobery Failure is high blowing off the fusible plugresulting in longer shut down and production lossBWLC fails to detect no water level. Further
avoids blowing of the Fusible plug & one canrestart quickly after trouble shooting.
resulting in longer shut down and production loss.
Highly reliable Micro switches of Highamperage for BWLC with safeties of Low waterAlarm and no water trip.
Low Ampere micro switches are used for BWLC.
Q i k M i tQuick Maintenance
Hinged rear refractory for quick easy openingwith one averagely skilled operator.
Rear Refractory is directly bolted and very difficultto remove.
Smoke box door clamping arrangements isrobust & leakfree. Smoke boxes can be opened& closed within 5 minutes.
The clamping arrangement requires frequentbreaking of clamps and opening of the doorrequires lot of time.
Special design of removable water feed pipe.This ensures that no “Cyclic Heating Cooling”stresses occur on the feed pipe welding onboiler shell. These stresses are induced whenthe feed pump starts pumping water at atemperature of 90 Deg.C cooling the weldingjoint and gets heated to Saturation temp of
Feed pipe is directly welded to the boiler shellhence the stresses are included due to coolingand heating of the welding joint during feed pumpON/OFF.
Steam when the Pump Stops.
Robust, easy to open & seal smoke boxes. Bulky and heavy design of smoke boxes.
Low Radiation Loss
Factory insulated low heat loss smoke boxes.S k b & it d i l t d ith
Refractory lined high heat loss smoke boxes.Smoke box & its doors are insulated withrockwool minimize rigid mattress to radiationlosses and doors are light weight.
y g
Dependable Bought-out Component Makes Delicate & yet expensive B.O. items
Electrical Load
Connected Electrical Load in Kw for 95% Efficient Steam Boiler (10.54 Kg/cm2)
1000 1500 2000 2500 3000 4000 5000 6000 8000 10000 12000 14000Model : Steamstar
1000 1500 2000 2500 3000 5000 6000Steam output (F & A 100 Deg.C) 4000 8000 10000 12000 14000
Blower
Feed Water Pump
Fuel Pump
Electric F. O. Heater
9.3
5.5
2.2
18
15
5.5
2.2
18
15
5.5
2.2
18
18.6
7.5
3.7
18
22.3
7.5
3.7
18
30
9.3
3.7
18
37.3153.718
3.7
3.7
1.1
12
3.7
3.7
1.1
12
3.7
3.7
1.1
12
5.5
3.7
1.1
12
5.5
3.7
1.1
12
Connected Electrical Load in Kw for 89% Efficient Steam Boiler (10.54 Kg/cm2)1000 1500 2000 2500 3000 4000 5000 6000 8000 10000 12000 14000Model : Steamstar
1000 1500 2000 2500 3000 5000 6000Steam output (F & A 100 Deg.C) 4000 8000 10000 12000 14000
Blower 9.3 11.25 11.25 15 18.6 22.3 3015
3.7 3.7 3.7 3.7 5.5
Steam to Fuel Ratios
Feed Water Pump
Fuel Pump
Electric F. O. Heater
5.5
2.2
18
5.5
2.2
18
5.5
2.2
18
7.5
3.7
18
7.5
3.7
18
9.3
3.7
18
153.718
3.7
1.1
12
3.7
1.1
12
3.7
1.1
12
3.7
1.1
12
3.7
1.1
12
GRAPH SHOWING STEAM TO FUEL RATIO AT VARIOUS FEED WATER TEMPERATURE
17 417.7
18
KG
14 715
15.315.615.916.216.516.817.117.4
UEL
RA
TIO
IN K
G/K Fuel : Furnace Oil
NCV : 9710 Kcal/Kg.Steam Pressure : 10 Kg./Cm2 (g)
89 % Efficient 93 % Efficient
12 312.612.913.213.513.814.114.414.7
STEA
M T
O F
U
95% Efficient
93 % Efficient
95% Efficient 93% Efficient 89% Efficient
1212.3
50 60 70 80 90 100 110 120 130 140FEED WATER TEMPERATURE IN DEG.C
Electrical LoadSteam to Fuel Ratios
GRAPH SHOWING STEAM TO FUEL RATIO AT VARIOUS FEED WATER TEMPERATURE
16.516.817.117.417.7
1818.318.6
O IN
KG
/KG
Fuel : Light Diesel Oil NCV : 10210 Kcal/Kg.Steam Pressure : 10.56 Kg./Cm2 (g)
13.814.114.414.7
1515.315.615.916.2
6 5
AM
TO
FU
EL R
ATI
O
89 % Efficient
95% Efficient
12.612.913.213.5
3 8
FEED WATER TEMPERATURE IN DEG.C
STEA
12.312
10 20 30 40 50 60 70 80 90 100 110 120 130 140
95% Efficient 89% Efficient
GRAPH SHOWING STEAM TO FUEL RATIO AT VARIOUS FEED WATER TEMPERATURE
18 8
15.616
16.416.817.217.6
1818.418.8
RA
TIO
IN K
G/K
G
95 % Efficient
Fuel : High Speed Diesel NCV : 10280 Kcal/Kg.Steam Pressure : 10.54 Kg./Cm2 (g)
1212.412.813.213.6
1414.414.815.2
5 6
STEA
M T
O F
UEL
R
89% Efficient
95% Efficient 89% Efficient
12
FEED WATER TEMPERATURE IN DEG.C
10 20 30 40 50 60 70 80 90 100 110 120 130 140
Steam Pressure Graph
GRAPH SHOWING STEAM GENERATION V/S FEED WATER PUMPSteam Pressure of 10.54 Kg./Cm2 (g)
FOR
AC
TUA
L C
APA
CIT
Y
1.1000
1.0500
1.0000
0.9500
ULT
IPLI
CA
TIO
N F
ACTO
R F
10 20 30 40 50 60 70 80 90 100 110 120 130 140
0.9000
0.8500
0.8000
0.7500
FEED WATER TEMPERATURE IN DEG.C
MU 10 20 30 40 50 60 70 80 90 100 110 120 130 140
Scope of SupplyScope of Supply for Control Panel and DocumentationPart Description QtyPart Description QtyControl Panel completely prewired for Automatic Operation consisting of ----Contactor & Overload Protection Relays for MotorRotary Selector SwitchesBoiler “START” Push ButtonBurner Prepurge Timer
1 No. each1 Set1 No1 No
Flame Failure Safety cum Burner Sequence Controller.Indicating bulbs with Name Plates for visual indication of various control modesmentioned above. (mounted on panel front)MCB for Control circuit Safety.Ignition Transformer.Contractor for Oil Heater.Digital Temperature Indicator cum switch for tube overheat safety
1 Set1 Set
1 No1 No1 No1 NoDigital Temperature Indicator cum switch for tube overheat safety.
Digital Temperature Indicator sum controller for Furnace oil heater.
Documentation :Operating & Maintenance Manual with B. O. Manuals Wiring DiagramInstallation Diagram viz. G. A. Drawing of Boiler & Foundation Location Drawing & P&I Diagram for Boiler
1 No1 No
1 Set
Drawing & P&I Diagram for Boiler.Things to be arranged at customers end.IBR Inspection Folder.Instruction Sheet on Installation, Erection & Commissioning for Equipment.Recommended Spare-parts list for Equipment for 2 years operations.
P & I Diagram
WILL BE SUPPLIED ONLY IF95% BOILER IS ORDERED
NEEDLE VALVEGLOBE VALVENONRETURN VALVEDAMPERSOLENOID VALVEGAUGE GLASS COCKSAFETY VALVEMOTORMECHNANICAL LINKAGEELECTRICAL SIGNAL
TESPL’S SUPPLYCLIENT’S SUPPLYSTACK TEMP. CONTROLLERTEMPERATURE ELEMENTTEMPERATURE INDICATORPRESSURE INDICATORAIR PRESSURE INDICATORAIR PRESSURE SWITCHPRESSURE SWITCH
PRESSUTROLPHOTOCELLLEVEL SWITCH (MOBREY)LEVEL INDICATORBLOW DOWN VALVEBOILER FEED WATERTUBE OVER HEAT TEMP. CONTROLLERAIR PRESSURE SWITCH
95% BOILER IS ORDERED.
P & I DIAGRAM FOR AIR & FLUE GAS CIRCUIT FOR SMOKE TUBE BOILERU O
NEEDLE VALVE
CONTROL VALVE
GLOBE VALVEBALL VALVENON RETRN VALVE
DAMPER
AUX. CUMVENT LINE
TO F. O. Steam Heater
Main SteamLine
To Chimney
FILTER
SOLENOID VALVE
GAUGE GLASS COCK
SAFETY VALVE
PLUG
TESPL’S SUPPLY
CLIENT’S SUPPLY
ELECTRICAL SIGNALINSTRUMENT AIR SIGNAL
TEMPERATURE ELEMENT
TEMPERATURE INDICATORPRESSURE INDICATOR
BOILER
PRESSURE INDICATORAIR PRESSURE INDICATOR
MOTOR
PRESSUTROL
PRESSUTROLPHOTOCELLLEVEL SWITCH (MOBREY)
LEVEL INDICATORBLOW DOWN VALVEBOILER FEED WATER
TEMP. INDICATOR / CONTROLLER
WATER PRE-HEATERMANONETREIC PR INDICATOR
WILL BE SUPPLIEDONLY IF 95% BOILER
IS ORDERED
To Blow Down Pit
InstrumentQualityCompressedAir InletPressure4 kg /cm2(g)
Steam Inlet
To Chimney
MANONETREIC PR. INDICATOR
From
Fee
dW
ater
Tan
k
Condensate Outlet
P & I DIAGRAM FOR FEED WATER AND STEAM CIRCUIT FOR SMOKE TUBE BOILER
P & I Diagram
BURNER
Steam FromAux. LineOf Boiler
CompressedAir at
Kg / cm2(g)
BURNER
BPRV
FOP 02
Fuel Pump 1
Vent LineTo F. O. Tank
Vent
Vent
Fuel FromF. O. Tank
F. O. Preheater(Steam)
FOP
07
Drain
FOP
04
05
Vent
ToDrain
F. O. PreheaterDrain
FOP 02
FOP 03
Fuel Pump 2
FOP
06FO
P 0
6
Drain
FOP 01
FOP
0
LEGENDSBURNER MANUFACTURERTESPL’S SUPPLYGEAR PUMPLOCAL MOUNTEDPANEL MOUNTEDORIFICE PLATE ASSEMBLYPLUGNEEDLE VALVEGLOBE VALVEBALL VALVESIMPLEX FILTERSOLENOID VALVE
PISTON OPERATED
TESPL’S SUPPLYCLIENT’S SUPPLYBACK PRES. REGULATING VALVEINLET PRES. REGULATING VALVEPHOTOCELLPRESSURE INDICATORPRESSURE SWITCHLEVEL INDICATORSTEAM TRAPELECTRICAL SIGNALINSTRUMENT AIR SIGNALTEMPERATURE ELEMENTTEMP INDICATING CONTROLLER
P & I DIAGRAM FOR FLUE OIL CIRCUIT FOR SMOKE TUBE BOILERPISTON OPERATED
CONTROL VALVETEMP. INDICATING CONTROLLERFUEL PRESSURE SWITCH BOILER
CompressedAir Inlet 4
CylinderPneumatic
TestAux. LineCum Vent
Line
ToF. O. Steam
Heater Main SteamLine
BURNER
Front Side
BOILER
WILL BE SUPPLIED ONLY IF95% BOILER IS ORDERED.
Signal From TICWater Preheater
From W.P.H.
To BPRV
LEGENDSNEEDLE VALVEGLOBE VALVE
TESPL’S SUPPLYCLIENT’S SUPPLY
PRESSUTROLPHOTOCELL
NONRETURN VALVEDAMPERSOLENOID VALVEGAUGE GLASS COCKSAFETY VALVEMOTORMECHANICAL LINKAGEELECTRICAL SIGNAL
STACK TEMP. CONTROLLERTEMP. ELEMENTTEMP. INDICATORPRESSURE INDICATORAIR PRESSURE INDICATORAIR PRESSURE SWITCHPRESSURE SWITCH
LEVEL SWITCH (MOBREY)LEVEL INDICATORBLOW DOWN VALVEBOILER FEED WATERTUBE OVER HEAT TEMP. CONTROLLERAIR PRESSURE SWITCH
P & I DIAGRAM FOR AIR & FLUE GAS CIRCUIT FOR SMOKE TUBE BOILER
Installation Photographs
Smoke Tube Boiler
Smoke Tube Boiler
14 TPH Steam Boiler Installed at Alkyal Amines
Smoke Tube Boiler
Heating Pumping Unit
Rear view of Smoke Tube Boiler
Installed Control Panel
Control Panel Burner
Control Panel Interior on Steam Star coil type Boiler
Control Panel Interior Control Panel Interior
Transparent Group of CompaniesTransparent Group Companies, are technology leaders working in the field of Co-generationSystems( CHP), Ammonia Absorption Refrigeration Plants (AARP), Waste Heat Recovery Systems,Energy Conservation Contracts, Biomass Gasification, Water Recycling Plants. Superefficient Boilers, Energy and Water consultancy, Pollutioncontrol, Drying Plants , Noise abatement Systems etc. having Indian Patents for many of its products.
Our company was incorporated on 16th April, 1986 with the name of Vapor Energy Machines Private Limited. The first commercial production was started in January, 1988. The name of the company was changed from Vapor Energy Machines Private Limited to Transparent Energy Systems Private Limited on 18th
December, 1995.
1. Waste Heat Recovery Systems 2. Waste Heat driven Power Plants3. Co-generation Systems
Transparent Energy Systems Private Limited www.tespl.com
4. Ammonia Absorption Refrigeration Plants - Technical collaboration and know-how transfer agreement with Mattes Engineering GmbH, Germany. www.mattes-int.com
5. Power Boilers - Technology licensing and know how transfer agreement with LaMont – Kessel GmbH, & Co, Germany www.lamont-services.com
6. Rankine Cycle Power Plants7. Air Cooled Steam / Vapour Condensers & Coolers8. Process Boilers & Heaters9. Combustion Turbine Inlet Air Cooling System - Co-operation understanding with The Cool Solutions Company, USA g y p g p y
www.coolsolutionsco.com10. Biomass Gasification Plants - Technology licensing & knowhow transfer agreement with Bioenergie Beratung Bornim GmbH, Germany -
www.b3-bornim.de11. Zero Liquid Effluent Discharge Plants12. Lithium Bromide Absorption Chillers - Co- operation agreement for application engineering, sales & service with Jiangsu Shuangliang Air-
Conditioning Equipment Co. Ltd., China www.shuangliang.com13. Waste Incineration fired Power Plants 14. Energy & Water Conservation Consultancy14. Energy & Water Conservation Consultancy
Transparent Technologies Private Limited - www.ttpl.co.in; www.ecokleen.com1. Flue Gas Desulphurization 2. Air Pollution Control3. Dryers& Coolers4. Incineration and Calcining
6. Fume & Dust Extraction Plants7. Air Stripping Plants & Airborne Solvent Vapour Recovery Plants8. Thermal Oxidation System of Airborne Solvent Vaporus9. Granulators
5. Solvent Recovery 10. Bulk Material Handling
Decimin Control Systems Pvt. Ltd. - www.decimin.com1. Noise Abatement Products & Systems
Gianazza Transparent Engineering India Pvt. Ltd. - http://www.gianazza.com; www.gte.net.inwww.gte.co.in
Joint Venture between Gianazza Engineering Ltd. SRL (Italy) and Transparent Technologies Pvt. Ltd.1. Edible Oil and Biodiesel Plants
Ecosustain Energy Systems Pvt. Ltd. - www.ecosustainenergy.comCo Operation Agreement with ShandongQingeng Thermal Power Equipment Co. Ltd
1. Steam Turbine Generators 2 Steam Turbine Drives
3. Steam Condensers 2. Steam Turbine Drives
Ecosustain Technologies Pvt. Ltd. . - www.ecosustain.co.in1. Water Recovery and reuse from effluents 2. Turnkey solutions through CECIC
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