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Efficient Uses of Steam Energy in Textiles to Reduce Cost & Improve Productivity
2nd International Conference on Textile & Apparel, ICTA-2012
What We Do?
o Forbes Marshall is an ISO 9001 company specializing in the Field of Steam Engineering & Control Instrumentation
o We are working with steam for last 106 years and have our manufacturing facility in India and others in joint venture with Spirax Sarco, ARCA, Krohne, Codel & Vynce.
o We manufacture Steam Boiler (NG/Diesel/Solid fuel fired), Exhaust Gas Boiler and almost all the steam system accessories.
Energy Audit
o Forbes Marshall has an Energy Audit division having expertise in
specific fields.
oForbes Marshall has conducted over 100 detailed energy audits across
the industry covering each and every process including dyeing units,
washing units, denim plants etc.
o In each of our audits we identified the opportunity for savings ranging
from 20% to 30%.
o Successful implementation of our audit recommendations of these
plants has yielded significant improvements in Specific Fuel
Consumption (SFC).
Why Steam?
o Fuel used for generating steam accounts for about 50% of total utility cost.
o Scarcity of Natural Gas, increase in cost of fuel and hence the steam costs
oEffective steam management plays a role in
Fuel Savings - which can be leveraged for cost competitiveness . Reducing
fuel cost is the only route to cut costs substantially.
Product Quality – Maintaining proper steam parameters ensures product
quality, e.g. uniform colour, print, brightness etc.
Productivity -Improving batch timings on equipment.
Benchmarking where do we stand ?
Forbes Marshall studies of over 60
textile plants reveal differences in fuel
consumption within the industry.
39% difference in Specific Fuel
Consumption (SFC) between the best
and average plants.
The worst plant consumes more
than 3 times the amount of fuel as
compared to the best plant.
Why is the best plant the best ?
Differences in Specific Fuel Consumption (SFC) across
plants on account of:
Efficient steam generation
Optimized steam distribution & utilization
Recovering condensate & flash steam
Proper steam trapping
Comparative Study
Capacity (Kg)
Ideal Steam Consumption with Right Steam and condensate
loop (Without Heat Recovery/With Heat Recovery*
(Kg/Batch)
Actual Steam consumption (Kg/Batch)
Required Steam
Pressure (Barg)
Actual Steam
Pressure (Barg)
Batch time
(mins)
Max Gradient (°C/min)
Light Medium Dark Light Medium Dark
250 461/281 559/379 641/461 527 660 769 3.5 6-7 400-450 5
400 660/460 711/511 770/570 782 839 890 3.5 6-7 450-500 5
600 863/563 1227/927 1698/1398 907 1326 1950 3.5 6-7 500-550 5
750 1358/758 1817/1217 1922/1322 1585 1980 2160 3.5 6-7 550-650 5
1500 2227/1377 2490/1640 2769/1919 2531 2982 3187 3.5 6-7 650-700 5
Common issues found because of not adopting right steam engineering practices-
Not getting right pressure & temperature in the m/c Batch time goes high and product quality hampered Proper steam trapping is not in practice Running boiler at lower pressure Not using PRV before Process machine Not using temperature control Many of the time traps are bypassed Steam distribution system is not proper Steam mains are oversized or undersized Traps and valves leakage Insulation of Steam & Condensate line is not proper Not recovering condensate & flash steam Feed water temperature is ambient Boiler blowdown is manual
A 1/8 inch hole in
steam main can waste
15 tons of coal or 9
tons of fuel oil per
year.
Valve Leakage
A leaking 25 NB Thermodynamic Trap on a 7 bar line will lose steam at the rate of 18 kg/hr. This translates to a loss of more than 150 Tons of steam annually.
Steam is venting to the atmosphere
No Steam Trap / Group Trapping in Vertical Cylinder Dryer
General Practice in Vertical Dryers
Group trapping
4 bar(g)
Over heated
+ excess dried cloth
Recommended Hookup – Vertical Dryers
Existing Hookup – Soft Flow
Recommended Hookup –
Typical Steam Circuit:
Pan Pan
Boiler
Feed Pump
Feed Tank
Make-up Water
Vat
Condensate
Condensate
Steam
Steam
Steam Process Vessel
Space HeatingSystem
The Steam and Condensate Loop
Boiler100% Input Process
Distribution losses 5-7%
85%
Boiler losses 13 - 15%20% Condensate
60% Process use
So, for 1 Ton steam for process, fuel used equal to 1.67 Ton
Steam use in process – 60%
Different losses – 40%
Steam Generation
Two things are directly effect boiler steam generation –
- Boiler operating pressure & Feed water temperature
Poor boiler efficiency due to-
Fluctuating loads – improper loading on the boiler which can be
addressed by proper boiler selection, capacity, burner turndown, etc.
Absence of diagnostics to take corrective action – same can be
addressed by steam and oil flow metering, stack monitoring with boiler load
management and online efficiency check.
Manual Blow down - because of over blow down losses of money and
less blow down increases the risk of boiler life.
Cost of a Boiler – Oil/Gas fired
Steam to Fuel Ratio
Radiation
FuelFlow
Burner
Losses•Stack
•Enthalpy•Un Burnt
Boiler
Draft
Blow down
SteamFlow
Air
BOILER HOUSE DIVISON
What affects Fuel Bill?Excess Air %Feed Water
TemperatureStack temperatureUn burnt lossesNumber of On-OffsScaling on tubesSoot DepositionBlow down TDSMoisture in Fuel
What to Monitor inside Boiler House ?
1. Steam Flow
2. Steam Pressure
3. Fuel Flow
4. S: F ratio
5. Stack Temp
6. % O2 in Flue gas
7. Feed Water Temp
8. Blow down TDS
9. Furnace Pressure
Deviation in 2% oxygen Results in 1.5 % Excess Fuel Consumption
10 % Excess Blowdown will amount to 2 % Excess Fuel Consumption
Factuals
Boiler Efficiency Monitoring System
Radiation
FuelFlow
Burner Boiler
Draft
Blow down
SteamFlow
Air
In DirectEfficiency
= 100 - { + }+
+
Losses•Stack
•Enthalpy•Un Burnt
Boiler Efficiency
Fuel Scope for savings (%)
Gas 11.2 %
Liquid 11.8 %
Solid 17.1 %
• No Matter which fuel type you look at, the scope of savings is 10 % to 15 % at least.
• No boiler is an exception
Conclusion
Steam Distribution
High distribution loss across plants on
account of -
o Improper line sizing
o Improper insulation
o Improper line routing & condensate removal from steam lines
These losses can be addressed by -
o Proper design of the distribution network, i.e.; proper line sizing
without extra provisions for expansions
o Proper insulation and efficiency checking mechanism
o Proper condensate removal from steam lines
o Diagnostics – pressure and temperature gauges, steam flow
meters, etc.
Distribute Steam at High Pressure
This will have the following advantages:
– Smaller bore steam pipes needed and therefore less heat (energy) loss due to the smaller surface area.
– Lower capital cost of steam mains, both materials such as pipes, flanges and support work and labour.
– Lower capital cost of insulation (lagging).
– The boiler can be operated at the higher pressure corresponding to its optimum operating condition, thereby operating more efficiently.
– The thermal storage capacity of the boiler is increased, helping it to cope more efficiently with fluctuating loads, and a reduced risk of priming and carryover
Pipe Sizing
• Greater Cost• Greater Heat Loss• Greater Volume of Condensate
Formed
• Lower Pressure to Steam Users• Not Enough Volume of Steam • Water Hammer and Erosion
Waterhammer
Sagging Main
Slug of water from condensate
Vibration and noise caused by
waterhammer
Condensate
Relaying to Higher Level
SteamRelayto highlevel
Drain Points
30 - 50m
Fall 1/250
Steam Flow Flow
Proper Condensate Drain
Condensate
PocketSteam Trap Set25/30m
Cross Section
Cross Section
Steam Trap Set
Steam Flow
Steam Flow
• Correct
• Incorrect
Branch Connections
CorrectIncorrect
Steam Steam
Condensate
Drainage of Condensate from Steam Line
Steam Flow
Separator
Fig. Temperature profile across a heat exchange surface
Importance of Moisture Separator
Steam Utilization
Steam Trapping - o In most plants, trap selection is an issue on heating applications.o Group trapping on equipment also needs to be addressed.o Across textile plant audits and surveys we have conducted we find that only 50% of the installed traps are OK.
TD Traps are used in Process, it should be float trap
Disadvantages of TD:
-Intermittent discharge.
-Condensates not
removed properly, get
water logged.
-Increase steam
consumption by 8~10%
-Increase process time
By 25~30%
Ball Float Trap:Ensures proper removal of condensate from the process as soon as it forms. Recommended for process application.
Condensate & Flash Steam Recovery
o Huge gap between quantum of condensate being
recovered and potential for recovery observed across
all plants.
o Across many plants, boiler feed water temperature is
ambient and condensate is being drained.
o In plants where condensate is recovered, it is doing
using an electrical pump leading to loss of useful heat.
o Flash steam is normally not recovered and is vented.
Flash steam can be recovered and used for feed water
heating.
* This calculation is made for diesel fired boiler. Similarly it can be done for gas fired boiler.
oCondensate water contains 20% energy of steam. Returning condensate
improves the feed water temperature and thus lowers fuel bill.
o Returning condensate to feed water tank cuts the makeup water
requirements.
o The condensate returned does not need to undergo water treatment and
thus saving treatment cost.
o It has no TDS. It reduces the requirement of blowdown thereby
curtailing blowdown losses.
o Reduce the cost for oxygen scavenging chemicals, since the improved
temperature will reduce the amount of dissolve oxygen almost 75%.
Benefits of Condensate Recovery:
Energy Content in Dye Liquor Not considering losses the Process Heat Recovery in Dyeing m/c
45 %
15 %
Dye Bath LiquorCooling Water
Energy Content
Benefits of Dye Liquor Heat Recovery
o Recover heat from dye liquor 60~80 deg C from the dyeing
machine. Savings up to 15% in steam used for hot water preparation.
o Pre-heats process water to the dyeing machine. 1-2 extra batches
per week possible.
o Facilities low temperature discharge to ETP. Helpful for effluent
treatment.
o Eliminates pressure fluctuation of boiler.
Dye Liquor Heat Recovery System
Trap Management
• Selection of right Trap
• Bypass
• Leakage Stop Leakages Insulation Condensate Recovery Flash Steam Recovery Stop Blowdown Losses Feedwater tank Management
Stop Waste (12-15%)
Enconomy opportunities
Optimization ( 8-10%)
Waste Management
Steam Flowmetering
Dye Liquore Heat Recovery
Efficiency Optimisation
Liquor ratio control
Steam Pressure Control
Temperature Control
Instant Hot water supply
Dryness of Steam
Capacity Utilisation
Encon opportunities
Encon Opportunities
Boiler Efficiency Monitoring
Waste Heat Recovery Boiler from Generator
Thermic Fluid Generator-Efficiency % optimisation
Hot water from DG set Jacket
Optimization
Waste Management
Heat Recovery
(7-8%)
Our recommendations which included –
o Optimized steam generation
o Improved steam distribution system
o Proper selection and sizing of steam traps
o Better management of the process like installing
temprature & pressure controls
o Utilizing waste heat recovery
o Recovering condensate with flash steam to improve the
boiler performance
Copyright Forbes Marshall, 2006-07
Forbes Marshall has a Consultancy Division worked for the project design and consultancy for steam, water & air distribution system to make the industry energy efficient and sustainable.
Forbes Marshall has done Consultancy in many industries of Bangladesh. Few of them are, Hameem Denim, DBL, Ecotex, GMS composite, Graphics Textils, etc.
Copyright Forbes Marshall, 2006-07
One of Many Successes in Bangladesh!!Cutting
Down
CostsIndustry Knit ConcernLocation NarayangongSteam Usage Fabric Dyeing, Finishing & GarmentsFuel Gas
Before Energy Audit - -They have a requirement of 3~4 TPH boiler- Their machine was starving for steam
After Energy Audit & Implementing Recommendations –
Till now they have no shortage of steam and no requirement of steam boiler
Reason found : Wastage and leakage of steam in different points Condensate was not recovered Boiler was running under pressure Too much blowdown losses Live steam wastages from garments section.
Copyright Forbes Marshall, 2006-07
One of Many Successes! Cutting
Down
CostsIndustry Textile Processing UnitLocation Madhya PradeshSteam Usage In Process eqpt – Stenters, Back filling
M/cs, Calendar M/c etcFuel Wood
The objective - Improve SPFC from 0.33 kgs wood/mt cloth (Rs 0.66/ mt cloth).
Energy conservation recommendations implemented by customer -optimized fuel management – sizing. -Optimized steam generation-undertook better management of process like temp control. -optimized waste heat recovery -reduced losses on account of inappropriate / in-operational trapping
The Results?
0.27
0.28
0.29
0.3
0.31
0.32
0.33
0.34
Pre Audit Post Implementation
Kg
/Met
er c
loth
0.54
0.56
0.58
0.6
0.62
0.64
0.66
0.68
Rs/
Met
er c
lothThe SPFC came down to
0.28 Kg Wood/ Mt Cloth (Rs0.58/MtCloth)!!
One of Many Successes!
CuttingDown
CostsIndustry Textile Processing UnitLocation GujaratSteam Usage Yarn Dyeing M/csFuel HSD
The objective – Reduce Fuel Consumption
Energy conservation recommendations implemented by customer -Optimized steam generation-Reduced losses in steam distribution circuit-undertook better management of process like temp control. -optimized waste heat recovery – dye liquor, condensate & flash recovery.-reduced losses on account of inappropriate / in-operational trapping
The Results?
Customer Saves Rs 30 Lakhs/year!!Before After Audit
Fuel Consumption (lts/day) 1,150 820
Costs (Rs/day) 17,250 9,020
One of Many Successes!
CuttingDownCosts
One of Many Successes!
CuttingDownCosts
Find out where you stand!!! Get a free scoping study done by FM Experts
Fuel prices would
continue to spiral
upwards……. & so would
your losses!
The longer you wait…..
The more your losses
accumulate!
Bangladesh Office Address:
3rd Floor, Rupsha Tower, Kamal Ataturk Avenue,
Road -17, Banani C/A, Dhaka.
Email: [email protected]
Website: www.forbesmarshall.com
Thank You