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Vineeth C et al. Int. Journal of Engineering Research and Application www.ijera.com
Vol. 3, Issue 5, Sep-Oct 2013, pp.190-193
www.ijera.com 190 | P a g e
Impact of Condensate Recovery on Boiler Fuel Consumption in
Textile Sector
Vineeth C1
, M G Prince2
1
(PG Scholar, MES College of Engineering, Calicut University, Kerala)
2
(Assistant professor, Department of Mechanical Engineering, MES College of Engineering, Kerala)
ABSTRACT
Energy is one of the main cost factors in the textile industry. Especially in times of high energy price volatility,
improving energy-efficiency should be a primary concern for textile plants. There are various energy-efficiency
improving opportunities that exist in every textile plant, many of which are cost-effective. Energy consciousness
and environmental awareness have transformed condensate from an inexpensive byproduct of steam distribution
to a valuable resource that can substantially reduce operating costs. The flash steam generated can contain up to
half of the total energy of the condensate, hence flash steam recovery is also an essential part of an energy
efficient system. This paper provides information on the steam consumption and recovery technologies and
measures applicable to the textile industry. The paper includes case studies from various textile plants in sachin
GIDC (Gujarat) and also provides the range of saving under varying conditions.
Keywords: Condensate recovery, Flash steam, Steam consumption, Textile industry
I. INTRODUCTION
One of the textile manufacturing clusters in
India is located in Sachin GIDC (Gujarat). The
products primarily comprise synthetic saris & dress
materials and cotton dress materials. There are about
56 textile processing units in the cluster. Of the 56
units in the cluster, around 70% are integrated units
with facilities for both dyeing and printing, while the
remaining units have only dyeing facilities.
The textile industry, in general, is not
considered an energy intensive industry. However, the
textile industry comprises a large number of plants
which together consume a significant amount of
energy. The share of total manufacturing energy
consumed by the textile industry in a particular
country depends upon the structure of the
manufacturing sector in that country. The textile
industry uses large quantities of both electricity and
fuels. The share of electricity and fuels within the total
final energy use of any textile sector depends on the
production of the textile industry. For instance, in spun
yarn spinning, electricity is the dominant energy
source, whereas in dyeing and printing the major
energy source is fuels.
Fuel is one of the main cost factors in the
textile industry. Especially in times of high energy
price volatility, improving energy-efficiency should be
a primary concern for textile plants. There are various
energy-efficiency opportunities that exist in every
textile plant, many of which are cost-effective. Energy
consciousness and environmental awareness have
transformed condensate from an inexpensive
byproduct of steam distribution to a valuable resource
that can substantially reduce operating costs. The flash
steam generated can contain up to half of the total
energy of the condensate, hence flash steam recovery
is an essential part of an energy efficient system.
II. TEXTILE PROCESSES
It involves a generalized flow diagram
depicting the various textile processes that are
involved in converting raw materials in to a finished
product [1]. All of these processes do not occur at a
single facility, although there are some vertically
integrated plants that have several steps of the process
all in one plant. There are also several niche areas and
specialized products that have developed in the textile
industry which may entail the use of special
processing steps that are not shown in fig 2.1
The primary raw materials used in textile
manufacture are grey cloth, polyester yarn, and various
chemicals like soaps, caustics, and dyeing and
bleaching agents. Grey cloth usually contains many
colored impurities like minerals, waxes, proteins, and
so on, which are removed by scouring, bleaching and
shrinking. The fabric is then dyed and printed to get
the finished products. Scouring is usually carried out
in ‘soflina’ Machines, while bleaching and shrinking
are carried out in drum washers. Dyeing is mainly
carried out in jet dyeing machines and jigger
machines. Printing is usually carried out by
mechanized screen printing processes, i.e. flatbed
printing or rotary printing. After printing, the fabric is
passed through looping machines, hydro extractors and
‘Stenter’ machines that dry the fabric enable the
colours to set properly and restore the fabric’s width
RESEARCH ARTICLE OPEN ACCESS
Vineeth C et al. Int. Journal of Engineering Research and Application www.ijera.com
Vol. 3, Issue 5, Sep-Oct 2013, pp.190-193
www.ijera.com 191 | P a g e
Figure 2.1 Textile processes
III. STEAM CONSUMPTION IN TEXTILE
SECTOR
The textile units use both electricity and
thermal energy in their processes. Electricity is
primarily drawn from the grid, and used to operate
pumps, fans, drives and for lighting. Thermal energy is
mainly obtained from lignite coal, imported coal and
natural gas which are readily available. Coal and
lignite are primarily used as fuel in boilers for steam
generation, and NG is used in machinery like Stander
machines (for heat setting) and loop machines.
The steam required for different processes in textile
industry is given in Table 3.1 below
Table 3.1 % of steam requirements in each process
Machine Process Steam
required (%)
Washing
drum
Scouring/Bleac
hing
13-16
Soflina Bleaching 6-8
Jet machine Dyeing 34-42
Jigger Dyeing 6-8
Ironing
machine
Drying 4-6
Loop
machine
Drying 6-8
Breakdown of steam in textile industry is shown
below. The percentage of steam consumption in each
process depends upon the type of industry and number
of equipments. The significant proportion of steam is
used by jet machine, around 34 to 42%.
Figure 3.1 Breakdown of steam in textile industry
IV. ENERGY-EFFICIENCY
IMPROVEMENT OPPORTUNITIES IN THE
TEXTILE SECTOR
This analysis of energy-efficiency
improvement opportunities in the textile industry
includes both opportunities for retrofit/process
optimization as well as the partial replacement of the
current machinery with state-of-the-art new
technology. The methods mainly consist of recovery
of heat from condensate. To improve boiler feed water
temperature by recovering flash steam and condensate
from jet dyeing machines.
4.1 condensate recovery
The primary points of focus when
considering collection of condensate and return to the
steam system is the fuel consumption. In plant fuel
consumption is decrease by about 1% for every 6°C
rise in the boiler feed-water temperature. Return of
condensate also reduces water cost; water treatment
cost and reduces the pollution load.
4.2 flash steam recovery
Condensate is discharged through traps from
a higher to a lower pressure. As a result of this drop in
pressure, some of the condensate will then re-
evaporate into 'flash steam. The flash steam generated
can contain up to half of the total energy of the
condensate, hence flash steam recovery is an essential
part of an energy efficient system.
% flash steam=(SH-SL)/H*100 (1)
Where SH = Sensible heat in the condensate at the
higher pressure before discharge, SL = Sensible heat in
the condensate at the lower pressure to which
discharge takes place and H = Latent heat in the steam
at the lower pressure to which the condensate has been
discharged.
Presently the condensate from jet dyeing
machines is drained locally; thereby catering to huge
enthalpy loss. Condensate from jet machine is
recovered only. These is because of recovery of
condensate from other machine is not beneficial. The
Vineeth C et al. Int. Journal of Engineering Research and Application www.ijera.com
Vol. 3, Issue 5, Sep-Oct 2013, pp.190-193
www.ijera.com 192 | P a g e
amount of condensate and flash steam produced in
each industry is given in table
Table 4.1 Amount of condensate formed
Name of
industry
Total
steam
consump
tion
(kg/day)
Amount of
condensate
formed
(kg/day)
Amount of
flash steam
recovered
(kg/day)
Vipul 63319 37312 2101
Vaishali 55104 36247 2043
Shikhar 63200 14368 810
Sachin 54144 33444 1865
Rivaa 89010 36764 2691
Sankalp 23080 8333 470
Tejoday 48464 39609 2233
Manila 48980 25553 1441
Rainbw 53140 38787 2187
Vaibav 19527 10004 564
From the audit conducted in 10 textile
processing unit it is observed that nearly 5.9% of total
fuel consumption is wasted through condensate
drainage. ie, nearly a 7.1 T fuel is wasted per day. But
this is the case of 10 industries, considering whole
industry in the apparel park surat, nearly 40 T of coal
is wasted per day, which is equivalent to a price value
of 16 lac rupees.
Table 4.2 Total fuel saving in each industry
Name of
industry
Fuel
consump
tions
(kg/day)
Total
fuel
saving
(kg/day
Monetary
saving
(Rs/Annum)
Vipul 15000 1188.48 1247901
Vaishali 16000 1154.86 1212613
Shikhar 18000 457.80 480698
Sachin 9000 737.87 1106820
Rivaa 14000 889.14 1333714
Sankalp 9000 185.44 278827
Tejoday 12000 883.47 1325170
Manila 8500 569.98 854979
Rainbw 12000 865.15 1297727
Vaibav 7500 223.13 334699
As per the study conducted, the textile
industry in sachin GIDC has been consumed about 121
T of coal per day for steam generation. Through
condensate and flash steam recovery, the potential
reduction in fossil fuel consumption reduces and also
raise the temperature of feed water to 80-900
. The
impact of heat recovery on boiler fuel consumption in
textile plant is shown fig 4.1.
Figure 4.1 Impact on fuel consumption
Based on detailed studies carried in
industries, some of the boilers were found to be
inefficient and the efficiencies were found to be range
of 50 to 60%. The following technological gaps were
identified for low efficiency [3]: The boilers are of
single pass or two pass flue gas path system leading to
low heat transfer and high flue gas losses. High heat
losses from the gate and surface due to damaged
insulation and opening of the charging doors, No
control on fuel firing, Partial combustion leading to
un-burnt carbon. With heat recovery the efficiency of
boiler increases to 2 to 6%
Figure 4.2 Boiler efficiency
V. IMPLEMENTATION OF FLASH STEAM
SEPARATOR WITH CONDENSATE
RECOVERY PUMP
Flash steam recovery not only reduces
economic losses from the system, but it also reduces
the steam flow in condensate return systems. The
condensate flow out of the flash tank will have much
less flash steam. If the discharge is pumped and the
pressure is maintained greater than the flash vessel
pressure, no flash steam will result in the condensate
discharge piping. To manage this type of system, a
flow meter should be installed in the flash steam exit.
This steam flow should be monitored and recorded
with respect to appropriate variables. The primary
concern is to identify failed steam traps blowing
through. The steam will be passed through to the flash
steam outlet.[4]
Vineeth C et al. Int. Journal of Engineering Research and Application www.ijera.com
Vol. 3, Issue 5, Sep-Oct 2013, pp.190-193
www.ijera.com 193 | P a g e
During working the hot condensate from jet machine
is collected in a flash vessel, where flash steam is
seperated and feeded directly to feed water tank. And
remaning condensate is collected in tank. From
condensate tank it is feeded to feed water tank by a
pump.
Figure 5.1 Boiler with heat recovery system
VI. CONCLUSION
The techniques and technologies of heat
recovery from condensate are analyzed. Experiences
prove that in most cases heat recovery requires low
investment and has a low payback of normally less
than 1 year. By reusing the condensate, feed water
temperature increases to 900
. Reuse of condensate as
feed water significantly increases boiler efficiency. By
turning to heat recovery, significant cost savings can
be achieved.
REFERENCE
[1] Goyal Sandeep, “Energy Conservation in
Textile industry, LAP Lambert Academic
Publishing 2011
[2] Saad El-Din A. Energy conservation
potential of measurement & control systems
and energy saving equipment in textile
(dyeing) processes; (gujarat,2004).
[3] Sathaye, J, Price, L,e la Rue du Can, S
Assessment of Energy Use and Energy
Savings Potential in Selected Industrial
Sectors in India. Report No. 57293, Berkeley,
Berkeley National Laboratory, 2005
[4] Energy Manager Training (EMT).
Bestpractices/case studies– Indian industries,
energy-efficiency measures in Kanco
Overseas Gujarat; 2005
[5] Energy Manager Training (EMT), Best
practices/case studies – Indian industries,
energy-efficiency measures in Vardhman
Yarns & Threads LtdHoshiarpur; 2008.
[6] Prince Aravin, “Energy conservation in
textile industries &savings, Jun 11 2008

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  • 1. Vineeth C et al. Int. Journal of Engineering Research and Application www.ijera.com Vol. 3, Issue 5, Sep-Oct 2013, pp.190-193 www.ijera.com 190 | P a g e Impact of Condensate Recovery on Boiler Fuel Consumption in Textile Sector Vineeth C1 , M G Prince2 1 (PG Scholar, MES College of Engineering, Calicut University, Kerala) 2 (Assistant professor, Department of Mechanical Engineering, MES College of Engineering, Kerala) ABSTRACT Energy is one of the main cost factors in the textile industry. Especially in times of high energy price volatility, improving energy-efficiency should be a primary concern for textile plants. There are various energy-efficiency improving opportunities that exist in every textile plant, many of which are cost-effective. Energy consciousness and environmental awareness have transformed condensate from an inexpensive byproduct of steam distribution to a valuable resource that can substantially reduce operating costs. The flash steam generated can contain up to half of the total energy of the condensate, hence flash steam recovery is also an essential part of an energy efficient system. This paper provides information on the steam consumption and recovery technologies and measures applicable to the textile industry. The paper includes case studies from various textile plants in sachin GIDC (Gujarat) and also provides the range of saving under varying conditions. Keywords: Condensate recovery, Flash steam, Steam consumption, Textile industry I. INTRODUCTION One of the textile manufacturing clusters in India is located in Sachin GIDC (Gujarat). The products primarily comprise synthetic saris & dress materials and cotton dress materials. There are about 56 textile processing units in the cluster. Of the 56 units in the cluster, around 70% are integrated units with facilities for both dyeing and printing, while the remaining units have only dyeing facilities. The textile industry, in general, is not considered an energy intensive industry. However, the textile industry comprises a large number of plants which together consume a significant amount of energy. The share of total manufacturing energy consumed by the textile industry in a particular country depends upon the structure of the manufacturing sector in that country. The textile industry uses large quantities of both electricity and fuels. The share of electricity and fuels within the total final energy use of any textile sector depends on the production of the textile industry. For instance, in spun yarn spinning, electricity is the dominant energy source, whereas in dyeing and printing the major energy source is fuels. Fuel is one of the main cost factors in the textile industry. Especially in times of high energy price volatility, improving energy-efficiency should be a primary concern for textile plants. There are various energy-efficiency opportunities that exist in every textile plant, many of which are cost-effective. Energy consciousness and environmental awareness have transformed condensate from an inexpensive byproduct of steam distribution to a valuable resource that can substantially reduce operating costs. The flash steam generated can contain up to half of the total energy of the condensate, hence flash steam recovery is an essential part of an energy efficient system. II. TEXTILE PROCESSES It involves a generalized flow diagram depicting the various textile processes that are involved in converting raw materials in to a finished product [1]. All of these processes do not occur at a single facility, although there are some vertically integrated plants that have several steps of the process all in one plant. There are also several niche areas and specialized products that have developed in the textile industry which may entail the use of special processing steps that are not shown in fig 2.1 The primary raw materials used in textile manufacture are grey cloth, polyester yarn, and various chemicals like soaps, caustics, and dyeing and bleaching agents. Grey cloth usually contains many colored impurities like minerals, waxes, proteins, and so on, which are removed by scouring, bleaching and shrinking. The fabric is then dyed and printed to get the finished products. Scouring is usually carried out in ‘soflina’ Machines, while bleaching and shrinking are carried out in drum washers. Dyeing is mainly carried out in jet dyeing machines and jigger machines. Printing is usually carried out by mechanized screen printing processes, i.e. flatbed printing or rotary printing. After printing, the fabric is passed through looping machines, hydro extractors and ‘Stenter’ machines that dry the fabric enable the colours to set properly and restore the fabric’s width RESEARCH ARTICLE OPEN ACCESS
  • 2. Vineeth C et al. Int. Journal of Engineering Research and Application www.ijera.com Vol. 3, Issue 5, Sep-Oct 2013, pp.190-193 www.ijera.com 191 | P a g e Figure 2.1 Textile processes III. STEAM CONSUMPTION IN TEXTILE SECTOR The textile units use both electricity and thermal energy in their processes. Electricity is primarily drawn from the grid, and used to operate pumps, fans, drives and for lighting. Thermal energy is mainly obtained from lignite coal, imported coal and natural gas which are readily available. Coal and lignite are primarily used as fuel in boilers for steam generation, and NG is used in machinery like Stander machines (for heat setting) and loop machines. The steam required for different processes in textile industry is given in Table 3.1 below Table 3.1 % of steam requirements in each process Machine Process Steam required (%) Washing drum Scouring/Bleac hing 13-16 Soflina Bleaching 6-8 Jet machine Dyeing 34-42 Jigger Dyeing 6-8 Ironing machine Drying 4-6 Loop machine Drying 6-8 Breakdown of steam in textile industry is shown below. The percentage of steam consumption in each process depends upon the type of industry and number of equipments. The significant proportion of steam is used by jet machine, around 34 to 42%. Figure 3.1 Breakdown of steam in textile industry IV. ENERGY-EFFICIENCY IMPROVEMENT OPPORTUNITIES IN THE TEXTILE SECTOR This analysis of energy-efficiency improvement opportunities in the textile industry includes both opportunities for retrofit/process optimization as well as the partial replacement of the current machinery with state-of-the-art new technology. The methods mainly consist of recovery of heat from condensate. To improve boiler feed water temperature by recovering flash steam and condensate from jet dyeing machines. 4.1 condensate recovery The primary points of focus when considering collection of condensate and return to the steam system is the fuel consumption. In plant fuel consumption is decrease by about 1% for every 6°C rise in the boiler feed-water temperature. Return of condensate also reduces water cost; water treatment cost and reduces the pollution load. 4.2 flash steam recovery Condensate is discharged through traps from a higher to a lower pressure. As a result of this drop in pressure, some of the condensate will then re- evaporate into 'flash steam. The flash steam generated can contain up to half of the total energy of the condensate, hence flash steam recovery is an essential part of an energy efficient system. % flash steam=(SH-SL)/H*100 (1) Where SH = Sensible heat in the condensate at the higher pressure before discharge, SL = Sensible heat in the condensate at the lower pressure to which discharge takes place and H = Latent heat in the steam at the lower pressure to which the condensate has been discharged. Presently the condensate from jet dyeing machines is drained locally; thereby catering to huge enthalpy loss. Condensate from jet machine is recovered only. These is because of recovery of condensate from other machine is not beneficial. The
  • 3. Vineeth C et al. Int. Journal of Engineering Research and Application www.ijera.com Vol. 3, Issue 5, Sep-Oct 2013, pp.190-193 www.ijera.com 192 | P a g e amount of condensate and flash steam produced in each industry is given in table Table 4.1 Amount of condensate formed Name of industry Total steam consump tion (kg/day) Amount of condensate formed (kg/day) Amount of flash steam recovered (kg/day) Vipul 63319 37312 2101 Vaishali 55104 36247 2043 Shikhar 63200 14368 810 Sachin 54144 33444 1865 Rivaa 89010 36764 2691 Sankalp 23080 8333 470 Tejoday 48464 39609 2233 Manila 48980 25553 1441 Rainbw 53140 38787 2187 Vaibav 19527 10004 564 From the audit conducted in 10 textile processing unit it is observed that nearly 5.9% of total fuel consumption is wasted through condensate drainage. ie, nearly a 7.1 T fuel is wasted per day. But this is the case of 10 industries, considering whole industry in the apparel park surat, nearly 40 T of coal is wasted per day, which is equivalent to a price value of 16 lac rupees. Table 4.2 Total fuel saving in each industry Name of industry Fuel consump tions (kg/day) Total fuel saving (kg/day Monetary saving (Rs/Annum) Vipul 15000 1188.48 1247901 Vaishali 16000 1154.86 1212613 Shikhar 18000 457.80 480698 Sachin 9000 737.87 1106820 Rivaa 14000 889.14 1333714 Sankalp 9000 185.44 278827 Tejoday 12000 883.47 1325170 Manila 8500 569.98 854979 Rainbw 12000 865.15 1297727 Vaibav 7500 223.13 334699 As per the study conducted, the textile industry in sachin GIDC has been consumed about 121 T of coal per day for steam generation. Through condensate and flash steam recovery, the potential reduction in fossil fuel consumption reduces and also raise the temperature of feed water to 80-900 . The impact of heat recovery on boiler fuel consumption in textile plant is shown fig 4.1. Figure 4.1 Impact on fuel consumption Based on detailed studies carried in industries, some of the boilers were found to be inefficient and the efficiencies were found to be range of 50 to 60%. The following technological gaps were identified for low efficiency [3]: The boilers are of single pass or two pass flue gas path system leading to low heat transfer and high flue gas losses. High heat losses from the gate and surface due to damaged insulation and opening of the charging doors, No control on fuel firing, Partial combustion leading to un-burnt carbon. With heat recovery the efficiency of boiler increases to 2 to 6% Figure 4.2 Boiler efficiency V. IMPLEMENTATION OF FLASH STEAM SEPARATOR WITH CONDENSATE RECOVERY PUMP Flash steam recovery not only reduces economic losses from the system, but it also reduces the steam flow in condensate return systems. The condensate flow out of the flash tank will have much less flash steam. If the discharge is pumped and the pressure is maintained greater than the flash vessel pressure, no flash steam will result in the condensate discharge piping. To manage this type of system, a flow meter should be installed in the flash steam exit. This steam flow should be monitored and recorded with respect to appropriate variables. The primary concern is to identify failed steam traps blowing through. The steam will be passed through to the flash steam outlet.[4]
  • 4. Vineeth C et al. Int. Journal of Engineering Research and Application www.ijera.com Vol. 3, Issue 5, Sep-Oct 2013, pp.190-193 www.ijera.com 193 | P a g e During working the hot condensate from jet machine is collected in a flash vessel, where flash steam is seperated and feeded directly to feed water tank. And remaning condensate is collected in tank. From condensate tank it is feeded to feed water tank by a pump. Figure 5.1 Boiler with heat recovery system VI. CONCLUSION The techniques and technologies of heat recovery from condensate are analyzed. Experiences prove that in most cases heat recovery requires low investment and has a low payback of normally less than 1 year. By reusing the condensate, feed water temperature increases to 900 . Reuse of condensate as feed water significantly increases boiler efficiency. By turning to heat recovery, significant cost savings can be achieved. REFERENCE [1] Goyal Sandeep, “Energy Conservation in Textile industry, LAP Lambert Academic Publishing 2011 [2] Saad El-Din A. Energy conservation potential of measurement & control systems and energy saving equipment in textile (dyeing) processes; (gujarat,2004). [3] Sathaye, J, Price, L,e la Rue du Can, S Assessment of Energy Use and Energy Savings Potential in Selected Industrial Sectors in India. Report No. 57293, Berkeley, Berkeley National Laboratory, 2005 [4] Energy Manager Training (EMT). Bestpractices/case studies– Indian industries, energy-efficiency measures in Kanco Overseas Gujarat; 2005 [5] Energy Manager Training (EMT), Best practices/case studies – Indian industries, energy-efficiency measures in Vardhman Yarns & Threads LtdHoshiarpur; 2008. [6] Prince Aravin, “Energy conservation in textile industries &savings, Jun 11 2008