steam star- fired boilers

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 : [email protected] [email protected] : 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.




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.




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




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


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


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


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


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

steam star- fired boilers

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