DIL-TENTER KUMAŞ KURUTMA ve EN FİKSE MAKİNESİ

DIL-TENTER KUMAŞ KURUTMA ve EN FİKSE MAKİNESİ

DIL-TENTER KUMAŞ KURUTMA ve
EN FİKSE MAKİNESİ
DIL-TENTER FABRIC DRYING and
HEAT SETTING MACHINE
DMS 22
DİLMENLER MAKİNE SANAYİ
Dilmenler, Türkiye, İstanbul’da 1982 yılında kurulan DMS Dilmenler Makine Tekstil San. Tic. A.Ş. 30.000 m2 kapalı
üretim sahasında 250 kişilik kalifiye ekibi ile Tekstil Boyama ve Terbiye Makineleri alanında üretim yapmaktadır.
Dilmenler has been established in 1982 and continues to manufacture Textile Dyeing and Finishing Machinery
with a closed area of 30.000 m2 and a qualified staff of 250 people.
02
SERTİFİKALARIMIZ
CERTIFICATIONS
ISO 9001: 2008 Kalite Yönetim Sistemi,
EN ISO 3834-2 Metalik malzemelerin ergitme
kaynağı için kalite şartları,
97/23/EC Basınçlı Ekipmanlar Direktifi.
ISO 9001: Quality Management System,
EN ISO 3834-2 Quality Conditions for
welding metallic equipments.
97/23/EC Pressure Equipment Directive.
DIL-TENTER KUMAŞ KURUTMA ve EN FİKSE MAKİNESİ
DIL-TENTER FABRIC DRYING and HEAT SETTING MACHINE
22
DIL-TENTER Kumaş Kurutma ve En Fikse Makinesi
Fonsiyonel ve ergonomik dizaynı saye-sinde teknolojinin geldiği en son noktada yüksek sistem ısıl verimli 62,8 - 85% proses
uygular.
Proses:
Kurudan veya Yaştan Fikse, Boya sonrası Kurutma, kurudan apreleme, yaştan apreleme, kaplama sonrası kurutma proseslerine
hizmet eder.
Çalışma Eni:
1600-2000 mm Dokuma
2000-2400 mm Örgü Kumaş
3000-3400 mm Ev Tekstili Dokuma Kumaş
3400-4000 mm Dokusuz Yüzey ve Halı
Kabin Sayısı: min. 4 - max.12 kabinli
Isıtma Sistemi: Gaz, Kızgınyağ, Buhar
Üretim Hızı : 5-120 m/min
DIL-TENTER Fabric Drying and Heat Setting Machine
Is economically and ergonomically designed with latest technological achievements and it is with up to 62,8 - 85 % of calorific
efficiency.
Process:
Heat setting from wet or dry fabric, drying after dyeing, impregnating from dry fabric, impregnating from wet fabric, drying after
coating or lamination.
Working width:
1600-2000 mm woven fabric,
2000-2400 mm for knitted fabric,
3000-3400 mm for home textile woven fabric,
3400-4000 mm nonwoven and carpet.
No of Chamber: min 4 - max 12 chamber
Heating system: Natural gas, thermic oil, steam
Production speed: 5-120 m/min
03
GİRİŞ BÖLÜMÜ
22
ENTRY UNIT
Giriş bölümü
Dokuma kumaşlar için;
mekanik fren,
hız ayarlı baskılı çekici,
balerinli J-box,
pnömatik frenli yüksek girişli silindir,
çiftli motorize pozisyon ayarlı açıcı silindir grubu,
salıncaklı tip ortalayıcı ve full bant sensörü fulara
yönlendirme silindiri.
Örgü kumaşlar için;
mekanik fren,
çiftli motorize pozisyon ayarlı açıcı silindir grubu,
hız ayarlı çıtalı ortalayıcı grubu
full bant sensörü ve yönlendirme silindirleri
04
Çekicili J-Box ve Salıncaklı Tip Ortalayıcı (Dokuma
Kumaş)
Entry section
For woven fabric,
mechanical brake,
speed adjusted pulling cylinder,
jbox and dancer roller,
High inlet with pneumatic brake,
Double opener with position adjustment
Dancer roller with full width sensor and directing roller
For knitted fabric,
mechanical bake,
Duble opener with position adjustment,
Segmented Guide roller with speed adjustment,
Full width sensor and directing rollers
Çıtalı Tip Ortalayıcı (Örgü Kumaş)
SIKMA FULARI
22
SQUEEZING PADDER
Sıkma Fuları
2 adet sıkma silindiri ve 80 litre
sıvı kapasiteli, seviye kontrollü
tank fular bölümüne monte
edilmiştir. Sıvı tankı tamamen
paslanmaz
sacdan
imal
edilmiştir.
Sıkma ünitesi 2 adet 300 mm
çaplı özel tip silindirlerden
oluşur. Silindir-lerden birisi
fular yan aynalarına kuvvetli
yataklarla monte edilmiştir.
Diğer silindir ise pnömatik
piston
vasıtasıyla
hareket
edebilir durumdadır. Bu ünite silindirlerin her noktasında
üniform bir basınç (50 N/mm)
Squeezing foulard
Squeezing
foulard
is
manufactured from complete
stainless steel with 2 squeezing
rollers and a liquid bowl with 80
lt of capacity and level control
system.
Squeezing unit consists of 2
polyurethane roller with 300
mm diameter. One of the roller
is fixed on the main frame of
foulard and the other one is
movable by means of pneumatic
pistons horizontally.
elde edilebilecek şekilde dizayn
edilmiştir.
Kumaş tansiyon kontrol silindiri,
kumaşın diğer fular veya
makinenin diğer kısımları ile
senkronize olarak çalışabilmesi
için fuların çıkış kısmına monte
edilmiştir.
Gerekli tüm pnömatik devre
elemanları
ve
boruları
yüklemeye dahildir.
Örme ve dokuma kumaş için
açıcı silindirler sisteme dahildir.
2. fular uygulamasında sıkma
basıncı 35 N/mm’dir.
System designed in such a way
that the nominal pressure is
obtained throughout the width of
the roller (50 N/mm)
Fabric tension control roller is
mounted on the exit side of the
foulard in order to synchronized
the foulard with the rest of the
machine. Squeezing pressure
is 35 N/mm in 2nd foulard
applications.
05
ZİNCİR GİRİŞ BESLEME BÖLÜMÜ
22
CHAIN ENTRY FEEDING UNIT
Makine giriş besleme sistemi
Operatör platformu ile beraber kumaş giriş ünitesi
Avansları ayrı ayrı ayarlanabilen her biri kendi hız kontrol cihazına sahip alt ve üst besleme silindirleri
Ana zincir üzerine +60%’a varan besleme imkanı
Paslanmaz malzemeden imal edilmiş, 2 adet açıcı silindir grubu ve manuel ayarlı atkı düzeltme sistemi.
Dokunmatik ekranlı Setex 848 TCE Kontrol Bilgisayarı ile makinenin tüm fonksiyonları kontrol edilir. Kumanda paneli açısal olarak sağ ve sola çevrilebilir.
6 m. uzunluğunda zincir giriş sistemi
İğne giriş sistemi
Sağ ve sol hız avansları ayrı ayrı ayarlanabilen
kenar iğneleme sistemi
Teflon sağ ve sol kumaş açıcıları ve iğne giriş
sistemi
Kumaş iğneleme fırçaları (2 adet sağ, 2 adet sol)
Kumaş Kenar Takip sensörleri
Zincir Kol en ayar sitemi
Kumaş enine göre ayarlanabilen V veya H tipi
buharlama ünitesi
IR Kenar Kurutma / IR Edge Drying
Kenar Kolalama Sistemi
Alttan kolalama sistemi.(Standart)
Üstten kolalama sistemi.(Opsiyonel)
IR kenar kurutma sistemi
Kenar kola sürülen kumaş kenarlarını kurutarak
pro-ses hızının muhafaza edilmesini sağlar.
06
Kenar İğneleme Besleme Sistemi / Edge pinning and feeding system
ZİNCİR GİRİŞ BESLEME BÖLÜMÜ
22
CHAIN ENTRY FEEDING UNIT
Machine Entry Fabric feeding system
Fabric Entry Unit with Operator platform
Top and bottom overfeeding rollers with separate speed and overfeeding control.
Overfeeding up to 60%
Manually controlled weft straightening unit with two individual opener roller.
Control cabinet equipped with Setex 848TCE touch screen controller.
Chain Entry section with 6 meters of chain
Fabric pinning entry
Fabric edge pinning system with separate right/
left speed adjustment
Fabric decurler before pinning in the entry
Fabric edge sensor
Fabric pinning wheels ( 2 nos at each side)
Chain width control system
V or H type steaming device adjusted according
to the width of the fabric.
Edge Gluing System
Bottom Gluing System (standard)
Top Gluing System (optional)
IR Edge Drying system
Edge of the fabric is dried after glue application in
order to keep the process speed constant.
Üstten Kololama sistemi / Top Gluing system
07
ISI KAMARALARI
22
THERMIC CHAMBERS
Kurutma & Fikse Isı Kabinleri
Çiftli hava sirkülasyonlu MULTI-AIR sistemli, manuel filitreli.
Ana sirkülasyon fanları alt üfleme ve üst üfleme ayrı ayrı
olmak üzere, performansları %50-100 arasında ayarlanabilir.
Isı yalıtımı 150mm kalınlığında kaya yönü ile sağlamıştır.
Hava sirkülasyon fanları her biri 7,5 kW/4p gücünde motorlara direkt akuple olarak bağlı 2 adet / kabin kullanılmıştır.
Prizmatik düzeli MULTI-AIR sistemi ile hava akışı alt ve üst
akış olarak bölünür ve kumaşın üzerinde daima homojen
hava sirkülasyonu yapılması sağlanır.
Makine durduğunda otomatik olarak kapanan pnömatik
tahrikli by-pass klapeleri ile hava üflemesi kesilir.
Servo sürücü kontrollü, dik veya yatık tip, zincir tahrik
sistemi
Epoxy tip, buhar ve neme dayanıklı elektrostatik boya
sistemi.
Zincir Sistemi
Dik zincir ; örgü modeli
Yatık zincir sistemi; örgü, dokuma ve denim üç ayrı model
Raylar özel çelikten imal edilmiş olup bakım gerektirmezler.
Pnömatik olarak zincir tansiyon kontrolü
Isıtma sistemi doğalgazlı, kızgın yağlı veya buharlı olabilir
Egzost vantilatörü; 40-100% performans ayarlanabilir
Zincir en ayar sistemi açma gerilimi 1000 kgf/lineer metre
kumaş (14 oz Denim kumaşa uygundur.)
Kurutma kabinlerinde, her biri 0.55 kW gücünde, 3 metre
eksen aralığında zincir en ayar sistemi mevcuttur.
Zincir çıkış kısmı için yine 0.55 kW gücünde 1 adet zincir en
ayar sistemi.
Termofikse Sistemi
Kabin içine monte edilen termofikse sensörleri kumaşın yüzey sıcaklığını ölçerek istenilen fikse zamanının
gerçekleştirilmesi için üretim hızının otomatik ayarlanmasını
sağlar. Ayrıca manuelde karar verilen sabit üretim hızında
kumaş yüzey sıcaklık dağılımının gözlenmesine imkan tanır.
Sistemin faydası proses kalitesini arttırma ve üretim artışıdır.
Egzost havası nem ölçümü ve kontrol sistemi
Double air circulation MULTI-AIR system with manual filters
Main blowers of 7,5 kw each with top and bottom air
circulation, separately controlled via inverter.
Isolation thickness of 150 mm with rock wool application.
Air circulation is divided for top and bottom with prismatic
nozzle system called MULTI-AIR in order to homogenous the
air coming from top and bottom as required.
Pneumatically controlled by-pass flaps in order to protect
the fabric in case of any stoppage
Vertical or horizontal chain system with servo drive
controlled.
Electrostatic epoxy paint resistant to steam and humidity
Chain system
Vertical chain for knitted fabric
Horizontal chain for woven, denim and home textile
materials
Chain rail produced with special steel for no maintenance
long life
Pneumatic chain tension control
Heating system of Natural Gas, Thermic oil and Steam
Exhaust fan, adjustable thorough exhaust humidity sensor
Chain width adjustment system with max opening tension of
1000 kgf/lineer meter fabric (suitable for 14 oz denim fabric)
Width adjustment system in each chamber (every 3 meters)
Thermo Setting system
Surface temperature of the fabric is measured by means of
heat setting sensors placed inside the heating chambers in
order to adjust the speed of the fabric to achieve the best
results of thermo setting of fabric. System also enable to
monitor the changes of surface temperatures at the desired
speed. Thermo setting system increases the process quality
and production with required results.
Exhaust Air Humidity Measurement and control system
System reduces the requirement of fresh air by 50 %.
Absolute humidity of the circulated air is measured by a
sensor (as kg H2O/kg dry air). In automatic mode, exhauts fan
speed is adjusted via inverter to catch the pre setted humidity
values. In manual mode, the changes in absolute humidty
would be monitored while the exhaust fan runs with fixed
speed. Up to 30% energy would be saved in drying process
with the system.
Egzoz nem kontrol sistemi, kurutma temiz hava gereksinimini
% 50 oranında azaltmaktadır. Bir sensör vasıtasıyla egzost
havası mutlak nemi (kg H2O/kg kuru hava) ölçülür. Manuel
veya otomatik olarak kullanılabilir. Otomatik modta set edilen
nem değerini gerçekleştirmek adına egzost fanı performansı
inverter ile ayarlanır. Manuel modta fan performansı karar
verilen değerde çalışır iken mutlak nem değeri gözlemlenir. Bu metodla kurutma pro-sesi en ekonomik şekilde
çalıştırılarak %30’lara varan enerji tasarrufu sağlar.
3612 kJ (860 kcal) per kg of water evoporated
Kurutma esnasındaki ısı tüketimi:
Edge Cutting system
Buharlaşan her kg su için yaklaşık 3612 kj (860 kcal)
System is used to slit the edge of the fabric after gluing
process with max speed of 120 m/min. Minimum wastage is
guaranteed by means of cutting disc movement with edge
sensor.
Kenar kesme sistemi
08
Drying and Heat Setting Chambers
Makineden çıkan kenar kolalı kumaşın kenarlarını kesmek
için kullanılır. Maksimum 120 m/min. üretim hızına kadar
kesme imkanı. Kenar takip sensörlü bıçak hareketi sayesinde
minimum mesafede kesme imkanı sağlar.
Heat consumption in drying
ISI KAMARALARI
22
THERMIC CHAMBERS
Horizontal Chain Type A
Horizontal Chain Type B
Vertical Chain
Düze Tasarımları / Nozzle Design
Type A
Type B
09
DIL-TENTER KUMAŞ KURUTMA ve EN FİKSE MAKİNESİ
DIL-TENTER FABRIC DRYING and HEAT SETTING MACHINE
Hava By-Pass klape tahrik Sistemi
10
En ayar tahrik sistemi ve mutlak enkoderi
Uçları açılabilen hava kanalları ile kolay ve hızlı düze temizliği
22
DIL-TENTER KUMAŞ KURUTMA ve EN FİKSE MAKİNESİ
DIL-TENTER FABRIC DRYING and HEAT SETTING MACHINE
Manuel kapak, Manuel Elek, Doğal Gazlı Isıtma Sistemli Kabin
22
11
PROSES ANALİZ 1
22
PROCESS ANALYSIS 1
ÖRGÜ KUMAŞ KURUTMA PROSESİ
DRYING PROCESS FOR KNITED FABRIC
Z = altitude
Number of Chamber
Machine Type
Fabric Type
Chamber Temperature
Weight of Fabric
Width of Fabric
Squeezing Effect( Last Foulard)
Weight Variation
Dry Fabric Outlet Humudity
Production Speed
Production Capacity
Water Evoparation per Hour
Contact Time
Exhaust Air " Absolute Humidity - Heat Efficiency"
30,0
With Heat Recovery;
66,7; 28,7
29,5
29,0
27,5
27,0
26,5
26,0
25,5
25,0
24,5
24,0
23,5
Heat Efficiency
28,0
[%]
28,5
Wet Fabric Inlet Temperature
Dry Fabric Outlet Temperature
Heat on the Wet Fabric
Heat on the Dry Fabric
23,0
22,5
77
76
75
74
73
72
71
70
69
E x h a u s t A i r A b s o l u t e H u m i d i t y w [ g H 2O/kg dry air]
68
67
66
Without Heat Recovery
Recovered Heat
22,0
Heat Recovery
61,0
54,0
53,0
52,0
51,0
50,0
With Heat Recovery;
66,7; 48
48,0
66
Absolute Humidity w
Exhaust Air mexhaust air
Fresh Air m2fresh air
47,0
Heat q2fresh air
Dry Bulb Temperature
Relative Humidity
Volumetric Fresh Air Need
Heat qEgzost Air
Exhaust Air
67
49,0
Combustion Air
Dry bulb Temperature
Relative Humidity
Combustion Air m1 fresh air
Heat q1 fresh air
Machine Body Heat Losses
Fresh Air for Burners
55,0
68
m/min
kg fabric/h
kg H2O/h
sec.
0
C
60
0
C
190
kcal/h
kcal/h
-16560
121980
kcal/h
kcal/h
549300
-109860
-20,00
%
Dry Bulb Temperature
Relative Humidity
Volumetric Flow Rate for Fresh Air
28,7
0,0800
0,2051
3
Sm /h
kcal/Sm3 gas
Pre-Heated Fresh Air
56,0
[ Sm3/h ]
57,0
70
69
w [ g H2O/kg dry air ]
%
%w
Gas Consumption
Gas Calorific Value
Heat Consumption
Heat Consumption Coefficent
Gas Consumption
58,0
74
73
72
71
Exhaust Air Absolute Humidity
%
Sm /kg fabric
59,0
75
cm
Gas Consumption Coefficient
60,0
76
190
264
196
39
9
0
25
600
234,0
72,0
0
C
g/m2
With Heat Recovery
µ%
Heat Efficiency
Exhaust Air "Absolute Humidity- Gas Consumption"
77
140
10
Stenter
Knitted 24/1 Single Jersey
meter
Sm3/kg H2O
3
48
kcal/h
kcal/kg H2O
m3/h
0
C
%RH
kg/h
kcal/h
kcal/h
g H2O/kg dry air
kg/h
kg/h
439440
1878
498
35
90
532
-15354
6811
66,7
7007
6475
6475
kcal/h
0
C
-296693
101,52
4,73
7362
639256
-186833
35
90
6055
529396
190,45
0,761
10360
132,27
3,338
9060
9155
%RH
m3/h
kcal/h
0
C
%RH
m3/h
MASS BALANCE
ENERGIE BALANCE
Heat Consumption
Recovery
kcal/h
Exhaust Air "Absolute Humidity - Flow Rate"
With
Heat
Heat consumption with
the fabric
350000 atık hava ile ısıl sarfiyat
11000
8000
7000
6000
Mass Flow
[kg/h]
5000
77
12
76
75
74
73
72
71
Exhaust Air Absolute Humidity
70
69
w [ g H2O/kg dry air ]
68
67
66
4000
[ xxxx/h ]
Fırın iç ısıl gücü
300000
içısıl gücü yüzdesi cinsinde ısı kaybı
Heat Energy [kcal/h]
9000
Exhaust Air Flow Rate
10000
Volumetric Flow
[m3/h]
kcal/h
kcal
%
0,0
0,0
105420,0
327208,7
51583
13,2
250000
200000
150000
100000
50000
0
Seri 1
Heat Loss
6811,3
Exhaust Air
327208,7
Dry Fabric
105420,0
DGHS Direct Gas Heated Stenter
Exhaust Air "Absolute - Relative Humidity"
0,5
0,4
0,3
0,2
0,1
77
76
75
74
73
72
71
70
69
68
Exhaust Air Absolute Humidity
w [g H2O/kg dry air]
25,5
25,3
25,1
24,9
24,7
24,5
24,3
0,0900
0,2308
0,0908
0,2327
0,0915
0,2347
0,0923
0,2367
0,0931
0,2386
0,0938
0,2406
0,0946
0,2426
54
54,46
54,92
55,38
55,84
56,3
9155
9155
9155
9155
9155
9155
67
66
0,0
Sm3/kg fabric
77
Without Heat
24,1
23,9 23,7
0,0954
0,2445
0,0961
0,2465
0,0969
0,2485
56,76
57,22
57,68
9155
9155
9155
76
75
74
73
72
71
Exhaust Air Absolute Humidity
Recovery
23,5 23,3
23,2
0,0977
0,2504
0,0984
0,2524
0,0992
0,2544
58,14
58,6
59,06
9155
9155
9155
23,0
70
69
68
w [ g H2O/kg dry air ]
Sm /kg fabric
59,52
60
9155
9155
Sm /h
kcal/Sm3 gas
3
Sm3/kg H2O
3
66
Gas Consumption Coefficient
Gas Consumption
Gas Calorific Value
498581
2131
502793
2149
507004
2167
511215
2185
515427
2203
519638
2221
523849
2239
528060
2257
532272
2275
536483
2293
540694
2311
544906
2329
549300
2347
560
35
90
599
-17273
14831
76,35
5436
4838
565
35
90
604
-17421
14957
75,55
5539
4935
569
35
90
609
-17568
15084
74,8
5639
5030
574
35
90
614
-17715
15210
74,05
5743
5129
579
35
90
619
-17862
15336
73,32
5848
5229
584
35
90
624
-18009
15463
72,62
5952
5328
588
35
90
629
-18156
15589
71,95
6055
5426
593
35
90
634
-18303
15715
71,3
6159
5524
598
35
90
639
-18451
15842
70,68
6261
5622
603
35
90
645
-18598
15968
70,07
6365
5720
607
35
90
650
-18745
16094
69,48
6469
5819
612
35
90
655
-18892
16221
68,91
6572
5917
617
35
90
660
-19039
16347
68,37
6673
6014
622
35
90
665
-19193
16479
67,798
6784
6119
kcal/h
kcal/kg H2O
m3/h
deg C
%RH
kg/h
kcal/h
kcal/h
g H2O/kg dry air
kg/h
kg/h
-139586
35
90
4524
530978
-142409
35
90
4615
538034
-145151
35
90
4704
545008
-147999
35
90
4796
552088
-150875
35
90
4890
559196
-153732
35
90
4982
566285
-156563
35
90
5074
573348
-159405
35
90
5166
580422
-162206
35
90
5257
587455
-165056
35
90
5349
594537
-167904
35
90
5441
601618
-170745
35
90
5534
608691
-173518
35
90
5623
615696
-176558
35
90
5722
623152
kcal/h
deg C
%RH
m3/h
kcal/h
Heat q2 Fresh air
190,00
0,868
8142
190,01
0,860
8287
190,09
0,850
8430
190,08
0,843
8575
190,04
0,836
8722
190,02
0,830
8868
190,03
0,823
9013
190,02
0,816
9158
190,05
0,809
9303
190,03
0,803
9448
190,02
0,797
9594
190,02
0,792
9739
190,06
0,785
9883
190,00
0,780
10037
deg C
%RH
m3/h
Dry Bulb Temperature
Relative Humidity
Volumetric Flow Rate for Fresh Air
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
54516
54275
27,6
27,2
500.000
Heat Energy
[ kcal/h]
450.000
386373,8
54051
27,9
53823
28,3
390458,7
HR-Total Heat Consumption;
439440
53600
28,6
394543,7
53386
29,0
398628,7
402713,6
53181
29,3
52982
29,7
406798,6
410883,5
52793
30,0
52606
30,4
414968,5
52424
30,7
105420,0
419053,5
105420,0
423138,4
105420,0
427401,0
Total Heat Consumption
52248
52083
with
31,0Exhaust Air 31,4
Internal Energy of Stenter
350.000
HR-with Exhaust Air
HR-with Exhaust Air; 327208,7
300.000
HR-with Fabric
250.000
HR-with Heat Loss
200.000
HR-Total Heat Consumption
150.000
HR-Internal Energy of Stenter
Dry Bulb Temperature
Relative Humidity
Volumetric Flow Rate for Fresh Air
Heat qexhaust air
MASS BALANCE
ENERGY BALANCE
Heat Consumption
Without Heat Recovery
400000
250000
200000
150000
100000
100.000
50.000
0
w Absolute Humidity
mexhaust air Exhaust Air
m2 Fresh Air
300000
Heat Loss
400.000
Combustion Air
Dry Bulb Temperature
Relative Humidity
Combustion Air m1 fresh air
Heat q1 fresh air
Heat Losses
51904
31,7350000
with Fabric
Heat Energy [kcal/h]
550.000
105420,0 Air
105420,0
105420,0 Humidity
105420,0
105420,0
105420,0
105420,0
105420,0
Exhaust
"Absolute
- Heat
Consumption"
105420,0
382288,8
Heat Consumption
Heat Consumption Coefficient
Fresh Air for Burners
494370
2113
105420,0
105420,0
600.000378203,9
374118,9
[ Sm3/kg ]
Heat Efficiency
µ%
0,1000
0,2564
67
Gas Consumption
0,6
Fresh Air
0,7
with heat recovery;
66,7; 0,761
H2O
0,260
0,250
0,240
0,230
0,220
0,210
0,200
0,190
0,180
0,170
0,160
0,150
0,140
0,130
0,120
0,110
0,100
0,090
0,080
0,070
Exhaust Air
0,8
Sm3/kg
Exhaust Air Relative Humudity
0,9
[ RH% ]
Exhaust Air Absolute Humidity-Gas Consumption
1,0
50000
66
67
68
69
70
71
72
Exhaust Air Absolute Humidity
73
74
w [ g H2O/kg dry air ]
75
76
77
0
Seri 1
Heat Loss
14831,1
Exhaust Air
374118,9
Dry Fabric
105420,0
13
PROSES ANALİZ 2
22
PROCESS ANALYSIS 2
ÖRGÜ KUMAŞ KURUTMA PROSESİ
DRYING PROCESS FOR KNITED FABRIC
Z = altitude
meter
140
Number of Chamber
10
Machine Type
Stenter
Fabric Type Knitted 28/1OE Vis. Full Lyc.Sprm.
0
Chamber Temperature
198
C
Weight of Fabric
g/m2
237
Width of Fabric
cm
181
Squeezing Effect( Last Foulard)
%
93
Weight Variation
%
47
Dry Fabric Outlet Humudity
%w
0
Production Speed
m/min
19
Production Capacity
kg fabric/h
552
Water Evoparation per Hour
513,4
kg H2O/h
Contact Time
sec.
94,7
370
350
330
310
290
270
250
230
210
190
E x h a u s t A i r A b s o l u t e H u m i d i t y w [ g H 2O/kg dry air]
170
150
130
59,0
58,0
57,0
56,0
55,0
54,0
53,0
52,0
51,0
50,0
49,0
48,0
47,0
46,0
45,0
44,0
43,0
42,0
Heat Efficiency
With Heat Recovery;
135,4; 58,1
[%]
Exhaust Air " Absolute Humidity - Heat Efficiency"
Wet Fabric Inlet Temperature
Dry Fabric Outlet Temperature
Heat on the Wet Fabric
Heat on the Dry Fabric
Without Heat Recovery
Recovered Heat
Heat Recovery
330
310
290
270
250
230
210
190
Exhaust Air Absolute Humidity
w [ g H 2O/kg dry air ]
170
150
130
[ Sm3/h ]
Gas Consumption
Gas Calorific Value
Heat Consumption
Heat Consumption Coefficent
Fresh Air for Burners
Combustion Air
Dry Bulb Temperature
Relative Humidity
Combustion Air m1 fresh air
Heat q1 fresh air
Machine Body Heat Losses
Absolute Humidity w
Exhaust Air mexhaust air
Fresh Air m2fresh air
Heat q2fresh air
Pre-Heated Fresh Air
Gas Consumption
72
71
70
69
68
67
66
65
64
63
62
61
60
59
58
57
56
55
54
53
52
51
50
Gas Consumption Coefficient
Exhaust Air
with heat recovery;…
350
C
60
0
C
198
kcal/h
kcal/h
-33120
116947
kcal/h
kcal/h
651378
-175318
-26,91
%
With Heat Recovery
µ%
Heat Efficiency
Exhaust Air "Absolute Humidity- Gas Consumption"
370
0
Dry Bulb Temperature
Relative Humidity
Volumetric Fresh Air Need
Heat qEgzost Air
Dry Bulb Temperature
Relative Humidity
Volumetric Flow Rate for Fresh Air
58,1
0,0942
0,1013
Sm3/kg fabric
Sm3/kg H2O
3
52
Sm /h
kcal/Sm3 gas
9155
476060
927
kcal/h
kcal/kg H2O
m3/h
0
C
%RH
kg/h
kcal/h
kcal/h
g H2O/kg dry air
kg/h
539
35
90
576
-16634
7379
135,4
5028
kg/h
4452
4452
kcal/h
0
C
-303773
189,41
0,41
6249
705261
-128454
35
90
4163
529942
%RH
3
m /h
kcal/h
0
C
198,05
81,50
%RH
3
m /h
1,193
8310
35,376
6255
MASS BALANCE
ENERGIE BALANCE
Heat Consumption
With Heat Recovery
kcal/h
Exhaust Air "Absolute Humidity - Flow Rate"
Heat consumption with the fabric
atık hava ile ısıl sarfiyat
450000,0
8000
7000
Volumetric Flow
[m3/h]
6000
5000
4000
3000
Mass Flow
[kg/h]
370
14
350
330
310
290
270
250
230
210
190
Exhaust Air Absolute Humidity
w [ g H2O/kg dry air ]
2000
1000
170
150
130
0
Fırın iç ısıl gücü
içısıl gücü yüzdesi cins. ısı kaybı
400000,0
kcal/h
kcal
%
83826,7
384854,4
70947
10,4
350000,0
Heat Energy [kcal/h]
9000
Exhaust Air Flow Rate
10000
[ xxxx/h ]
11000
0,0
0,0
300000,0
250000,0
200000,0
150000,0
100000,0
50000,0
0,0
Seri 1
Heat Loss
7378,9
Exhaust Air
384854,4
Dry Fabric
83826,7
DGHS Direct Gas Heated Stenter
Exhaust Air "Absolute - Relative Humidity"
Exhaust Air Absolute Humidity-Gas Consumption
1,4
1,3
1,2
1,1
with heat recovery;
135,4; 1,193
370
350
330
310
290
270
Exhaust Air Absolute
53,9
52,8
51,8
50,8
250
230
Humidity
49,8
210
190
170
w [g H2O/kg dry air]
48,9
48,0
0,1016
0,1093
0,1037
0,1115
0,1058
0,1138
0,1079
0,1160
0,1100
0,1183
0,1121
0,1205
0,1142
0,1228
56,1
57,257
58,414
59,571
60,728
61,885
9155
9155
9155
9155
9155
9155
150
130
1,0
0,125
0,120
0,115
0,110
Sm3/kg fabric
0,105
370
Without Heat
47,1
46,3 45,5
0,1163
0,1251
0,1184
0,1273
0,1205
0,1296
63,042
64,199
65,356
9155
9155
9155
350
330
310
290
270
250
230
Exhaust Air Absolute Humidity
Recovery
44,7 43,9
43,2
42,5
210
190
170
w [ g H2O/kg dry air ]
µ%
0,1226
0,1318
0,1247
0,1341
0,1268
0,1363
0,1289
0,1386
Sm3/kg fabric
66,513
67,67
68,827
69,984
71,15
9155
9155
9155
9155
9155
Sm /h
kcal/Sm3 gas
Sm3/kg H2O
3
150
130
0,100
Heat Efficiency
Gas Consumption Coefficient
Gas Consumption
Gas Calorific Value
524188
1021
534780
1042
545373
1062
555965
1083
566557
1104
577150
1124
587742
1145
598334
1166
608927
1186
619519
1207
630111
1227
640704
1248
651378
1269
582
35
90
622
-17945
15408
370,4
1523
594
35
90
635
-18315
15726
323,4
1770
606
35
90
648
-18685
16043
287,8
2017
618
35
90
660
-19055
16361
260,1
2264
630
35
90
673
-19426
16679
237,8
2510
642
35
90
686
-19796
16997
219,4
2759
654
35
90
699
-20166
17314
204,1
3006
666
35
90
712
-20536
17632
191,2
3251
678
35
90
725
-20906
17950
180
3500
690
35
90
737
-21276
18268
170,4
3745
702
35
90
750
-21646
18586
161,9
3992
714
35
90
763
-22016
18903
154,4
4239
726
35
90
776
-22386
19221
147,7
4488
738
35
90
789
-22759
19541
141,68
4737
kcal/h
kcal/kg H2O
m3/h
deg C
%RH
kg/h
kcal/h
kcal/h
g H2O/kg dry air
kg/h
901
1135
1370
1603
1837
2073
2307
2540
2775
3007
3242
3476
3712
3948
kg/h
-25997
35
90
843
458303
-32746
35
90
1061
475697
-39519
35
90
1281
493114
-46258
35
90
1499
510498
-53010
35
90
1718
527895
-59802
35
90
1938
545331
-66562
35
90
2157
562736
-73278
35
90
2375
580097
-80070
35
90
2595
597534
-86771
35
90
2812
614879
-93543
35
90
3032
632296
-100307
35
90
3251
649705
-107101
35
90
3471
667143
-113921
35
90
3692
684691
kcal/h
deg C
%RH
m3/h
kcal/h
Dry Bulb Temperature
Relative Humidity
Volumetric Flow Rate for Fresh Air
Heat qexhaust air
198,00
198,03
198,00
198,04
198,05
198,00
198,00
198,06
198,02
198,09
198,08
198,07
198,03
198,02
deg C
Dry Bulb Temperature
2,495
3298
2,285
3651
2,114
4004
1,969
4357
1,846
4710
1,743
5064
1,651
5418
1,569
5769
1,499
6124
1,434
6475
1,378
6829
1,327
7182
1,282
7537
1,239
7893
%RH
m3/h
Relative Humidity
Volumetric Fow Rate for Fresh Air
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
650.000
116190
600.000
13,3
108939
14,4
445184,6
102952
15,6
97955
16,7
455459,2
93700
17,8
465733,7
90022
18,9
476008,3
486282,9
86836
19,9
84056
21,0
496557,4
506832,0
81572
22,0
83826,7
527381,1
517106,6
79385
23,0
77405
24,0
83826,7
537655,7
Total Heat Consumption
75622
74000
with
25,0Exhaust Air 26,0
Heat Loss
[ kcal/h]
with Fabric
500.000
Heat Energy
550.000
450.000
300.000
HR-Total Heat Consumption;
476060
400.000
350.000
Internal Energy of Stenter
HR-with Exhaust Air
HR-with Fabric
HR-with Exhaust Air; 384854,4
HR-with Heat Loss
250.000
HR-Total Heat Consumption
200.000
HR-Internal Energy of Stenter
150.000
Combustion Air
Dry Bulb Temperature
Relative Humidity
Combustion Air m1 fresh air
Heat q1 fresh air
Heat Losses
w Absolute Humidity
mexhaust air Exhaust Air
m2 Fresh air
Heat q2 Fresh air
MASS BALANCE
ENERGY BALANCE
Heat Consumption
Without Recovery
450000,0
72519
400000,0
26,9
350000,0
300000,0
250000,0
200000,0
150000,0
100000,0
100.000
50.000
0
83826,7
548010,2
Heat Energy [kcal/h]
Exhaust
"Absolute
Humidity
- Heat
Consumption"
83826,7 Air
83826,7
83826,7
83826,7
83826,7
83826,7
83826,7
83826,7
83826,7
434910,0
Heat Consumption
Heat Consumption Coefficient
Fresh Air for Burners
513596
1000
83826,7
83826,7
700.000424635,5
414360,9
[ Sm3/kg ]
0,130
Sm3/kg H2O
Gas Consumption
1,7
1,6
1,5
0,135
Fresh Air
1,9
1,8
0,140
Exhaust Air
2,2
2,1
2,0
[ RH% ]
2,4
2,3
0,145
Exhaust Air Relative Humudity
2,6
2,5
50000,0
130
150
170
190
210
230
250
270
Exhaust Air Absolute Humidity
290
310
330
w [ g H2O/kg dry air ]
350
370
0,0
Seri 1
Heat Loss
15407,9
Exhaust Air
414360,9
Dry Fabric
83826,7
15
PROSES ANALİZ 3
22
PROCESS ANALYSIS 3
ÖRGÜ KUMAŞ KURUTMA VE TERMOFİKSE PROSESİ
DRYING AND HEATSETTING PROCESS FOR KNITED FABRIC
Z = altitude
Number of Chamber
Machine Type
Fabric Type
Chamber Temperature
Weight of Fabric
Width of Fabric
Squeezing Effect( Last Foulard)
Weight Variation
Dry Fabric Outlet Humidity
Production Speed
Production Capacity
Water Evoparation per Hour
Contact Time
Exhaust Air " Absolute Humidity - Heat Efficiency"
70
With Heat Recovery;
94; 68,1
68
64
62
[%]
66
58
56
54
52
50
48
Heat Efficiency
60
Wet Fabric Inlet Temp
Dry Fabric Outlet Temp
Heat on the Wet Fabric
Heat on the Dry Fabric
46
44
350
330
310
290
270
250
230
210
190
170
150
E x h a u s t A i r A b s o l u t e H u m i d i t y w [ g H2O/kg dry air]
130
110
90
Without Heat Recovery
Recovered Heat
42
Heat Recovery
85
65
60
130
m/min
kg fabric/h
kg H2O/h
sec.
0
C
60
0
C
115
kcal/h
kcal/h
-39984
89148
kcal/h
kcal/h
772133
-282340
-36,57
%
110
55
90
[ Sm3/h ]
Fresh Air for Burners
50
68,1
0,0787
0,0865
3
Sm /h
3
kcal/Sm gas
3
53,5
kcal/h
kcal/kg H2O
489793
792
m /h
0
C
%RH
kg/h
kcal/h
kcal/h
g H2O/kg dry air
555
35
90
593
-17113
7592
94
10195
Absolute Humidity w
Exhaust Air mexhaust air
Fresh Air m2fresh air
Sm3/kg H2O
9155
3
kg/h
kg/h
9602
9602
Dry Bulb Temperature
kcal/h
0
C
-559407
150,28
-277066
35
Relative Humidity
Volumetric Fresh Air Need
Heat qexhaust air
%RH
m3/h
kcal/h
1,06
12339
1009557
90
8979
727217
Heat q2fresh air
Exhaust Air
With Heat Recovery;
94; 53,5
190
170
150
w [ g H 2O/kg dry air ]
%
%w
Gas Consumption
Gas Calorific Value
Combustion Air
Dry Bulb Temperature
Relative Humidity
Combustion Air m1 fresh air
Heat q1 fresh air
Machine Body Heat Losses
Pre-Heated Fresh Air
70
290
270
250
230
210
Exhaust Air Absolute Humidity
%
Sm /kg fabric
Heat Consumption
Heat Consumption Coefficent
Gas Consumption
75
310
cm
Gas Consumption Coefficient
80
330
152
250
162
91
10
7
28
680
618,8
64,3
0
C
g/m2
With Heat Recovery
µ%
Heat Efficiency
Exhaust Air "Absolute Humidity- Gas Consumption"
350
140
10
Stenter
Knitted 28/1 OE Vis.Lyc.suprem
meter
Dry Bulb Temperature
Relative Humidity
Volumetric Flow Rate for Fresh Air
0
C
152,10
53,64
%RH
3
m /h
2,598
14375
88,651
11047
MASS BALANCE
ENERGIE BALANCE
Heat Consumption
With Heat Recovery
Exhaust Air "Absolute Humidity - Flow Rate"
Heat consumption with the fabric
500000,0 atık hava ile ısıl sarfiyat
15000
14000
10000
9000
8000
7000
6000
5000
4000
Mass Flow
[kg/h]
3000
2000
350
16
330
310
290
270
250
230
210
Exhaust Air Absolute Humidity
190
170
150
w [ g H2O/kg dry air ]
130
110
90
1000
Fırın iç ısıl gücü
iç ısıl gücü yüzdesi cinsinde ısı kaybı
400000,0
kcal
%
49164,0
433036,7
58711
12,9
350000,0
Heat Energy [kcal/h]
11000
Volumetric Flow
[m3/h]
450000,0
[ xxxx/h ]
12000
Exhaust Air Flow Rate
13000
kcal/h
kcal/h
0,0
0,0
300000,0
250000,0
200000,0
150000,0
100000,0
50000,0
0,0
Seri 1
Heat Loss
7591,8
Exhaust Air
433036,7
Dry Fabric
49164,0
DGHS Direct Gas Heated Stenter
Exhaust Air "Absolute - Relative Humidity"
Exhaust Air Absolute Humidity-Gas Consumption
62,2
60,5
58,5
56,7
55,0
53,4
51,8
0,0862
0,0947
0,0886
0,0974
0,0916
0,1006
0,0945
0,1039
0,0975
0,1071
0,1004
0,1104
0,1034
0,1136
58,6
60,266
62,2723
64,2784
66,28455
68,2907
9155
9155
9155
9155
9155
9155
110
90
0,100
Sm3/kg fabric
0,090
0,080
350
330
Without Heat
50,4
49,0 47,8
0,1063
0,1168
0,1093
0,1201
0,1122
0,1233
70,29685
72,303
74,30915
9155
9155
9155
310
290
270
250
230
210
190
170
150
130
Exhaust Air Absolute Humidity
w [ g H2O/kg dry air ]
Recovery
46,5 45,4
44,3
43,2
µ%
0,1152
0,1266
0,1181
0,1298
0,1211
0,1331
0,1240
0,1363
Sm /kg fabric
76,3153
78,32145
80,3276
82,33375
84,34
9155
9155
9155
9155
9155
Sm /h
3
kcal/Sm gas
3
Sm3/kg H2O
3
110
90
Heat Efficiency
Gas Consumption Coefficient
Gas Consumption
Gas Calorific Value
551735
892
570103
921
588469
951
606835
981
625201
1010
643568
1040
661934
1070
680300
1099
698667
1129
717033
1159
735399
1188
753765
1218
772133
1248
kcal/h
kcal/kg H2O
607
35
90
650
-18745
16094
339,25
2023
625
35
90
668
-19278
16552
279,01
2518
646
35
90
690
-19920
17103
231,93
3115
666
35
90
713
-20561
17654
200
3712
687
35
90
735
-21203
18205
176,91
4309
708
35
90
757
-21845
18756
159,43
4906
729
35
90
779
-22486
19307
145,75
5503
750
35
90
802
-23128
19858
134,75
6100
770
35
90
824
-23770
20409
125,7
6697
791
35
90
846
-24412
20960
118,14
7294
812
35
90
868
-25053
21511
111,725
7891
833
35
90
891
-25695
22062
106,21
8488
854
35
90
913
-26337
22613
101,42
9085
874
35
90
935
-26979
23164
97,22
9682
m /h
deg C
%RH
kg/h
kcal/h
kcal/h
g H2O/kg dry air
1373
1850
2425
3000
3574
4149
4724
5298
5874
6448
7023
7597
8172
8747
kg/h
-39616
35
-53391
35
-69974
35
-86551
35
-103132
35
-119723
35
-136304
35
-152880
35
-169479
35
-186058
35
-202634
35
-219216
35
-235797
35
-252381
35
kcal/h
deg C
Heat q2 Fresh air
90
1284
529585
90
1730
558688
90
2268
593730
90
2805
628763
90
3342
663801
90
3880
698849
90
4417
733887
90
4955
768920
90
5492
803976
90
6030
839012
90
6567
874045
90
7104
909084
90
7642
944122
90
8179
979164
%RH
m3/h
kcal/h
Relative Humidity
Volumetric Flow Rate for Fresh Air
Heat qexhaust air
152,01
152,01
152,01
152,01
152,01
152,01
152,01
152,01
152,01
152,01
152,01
152,01
152,01
152,01
deg C
Dry Bulb Temperature
7,000
3828
6,143
4468
5,388
5238
4,826
6008
4,392
6778
4,047
7548
3,766
8319
3,532
9089
3,335
9859
3,166
10629
3,020
11399
2,893
12169
2,781
12940
2,681
13710
%RH
3
m /h
Relative Humidity
Volumetric Flow Rate for Fresh Air
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
115657
700.000
13,9
49164,0
503835,8
104542
15,8
521650,7
94762
18,0
539466,0
87492
20,2
81873
22,2
557281,3
77398
24,2
575096,6
592911,9
73754
26,2
70728
28,1
610727,3
628542,6
68172
29,9
646357,9
65988
31,8
64101
33,6
Heat Energy
[ kcal/h]
600.000
HR-Total Heat Consumption;
489793
500.000
49164,0
699804,7
Total Heat Consumption
62451
60998
with Exhaust Air37,1
35,3
HR-Internal Energy of Stenter
200.000
Dry Bulb Temperature
500000
350000
HR-Total Heat Consumption
w Absolute Humidity
mexhaust air Exhaust Air
m2 Fresh air
59708
450000
38,8
400000
HR-with Heat Loss
Combustion Air
Dry Bulb Temperature
Relative Humidity
Combustion Air m1 fresh air
Heat q1 fresh air
Heat Losses
Heat Consumption
Without Heat Recovery
Heat Loss
HR-with Fabric
Heat Consumption
Heat Consumption Coefficient
MASS BALANCE
ENERGY BALANCE
with Fabric
HR-with Exhaust Air
300.000
300000
250000
200000
150000
100000
100.000
0
49164,0
681988,5
Internal Energy of Stenter
HR-with Exhaust Air; 433036,7
400.000
49164,0
664173,2
Heat Energy [kcal/h]
Exhaust
Air
"Absolute
Humidity
- Heat
Consumption"
49164,0
49164,0
49164,0
49164,0
49164,0
49164,0
49164,0
49164,0
49164,0
49164,0
800.000486019,2
471224,5
kg/h
[ Sm3/kg ]
0,070
536483
867
3
Gas Consumption
[ RH% ]
0,110
Fresh Air for Burners
310
290
270
250
230
210
190
170
150
130
Exhaust Air Absolute Humidity
w [g H2O/kg dry air]
0,120
Sm3/kg H2O
Fresh Air
330
0,130
Exhaust Air
350
0,140
Exhaust Air Relative Humudity
Dry Fabric outlet
Humidity [RH%];
339,25; 7
12,0
11,5
11,0
10,5
10,0
9,5
9,0
8,5
8,0
7,5
7,0
6,5
6,0
5,5
5,0
4,5
4,0
3,5
3,0
2,5
2,0
1,5
1,0
0,5
0,0
50000
0
90
110
130
150
170
190
210
230
Exhaust Air Absolute Humidity
250
270
290
w [ g H 2O/kg dry air ]
310
330
350
Seri 1
Heat Loss
16094,5
Exhaust Air
471224,5
Dry Fabric
49164,0
17
PROSES ANALİZ 4
22
PROCESS ANALYSIS 4
ÖRGÜ KUMAŞ KURUTMA VE TERMOFİKSE PROSESİ
DRYING AND HEATSETTING PROCESS FOR KNITED FABRIC
Z = altitude
Number of Chamber
Machine Type
Fabric Type
Chamber Temperature
Weight of Fabric
Width of Fabric
Squeezing Effect( Last Foulard)
Weight Variation
Dry Fabric Outlet Humudity
Production Speed
Production Capacity
Water Evoparation per Hour
Contact Time
Exhaust Air " Absolute Humidity - Heat Efficiency"
72
With Heat Recovery;
151; 69,1
70
66
64
[%]
68
60
58
56
54
52
50
48
Heat Efficiency
62
Wet Fabric Inlet Temperature
Dry Fabric Outlet Temperature
Heat on the Wet Fabric
Heat on the Dry Fabric
46
44
225
220
215
210
205
200
195
190
185
180
175
170
E x h a u s t A i r A b s o l u t e H u m i d i t y w [ g H2O/kg dry air]
165
160
155
150
Without Heat Recovery
Recovered Heat
42
Heat Recovery
60
205
200
195
190
185
180
175
170
165
Exhaust Air Absolute Humidity
w [ g H 2O/kg dry air ]
160
155
55
150
%
%w
m/min
kg fabric/h
kg H2O/h
sec.
0
C
60
0
C
115
kcal/h
kcal/h
-41530
86554
kcal/h
kcal/h
645428
-141903
-21,99
%
Sm /h
3
kcal/Sm gas
Combustion Air
Dry Bulb Temperature
Relative Humidity
Combustion Air m1 fresh air
Heat q1 fresh air
Machine Body Heat Losses
Absolute Humidity w
Exhaust Air mexhaust air
Fresh Air m2fresh air
Heat q2fresh air
69,1
0,0818
0,0853
3
Gas Consumption
Gas Calorific Value
Fresh Air for Burners
50
Exhaust Air
With Heat Recovery;
151; 55
210
%
Sm /kg fabric
Pre-Heated Fresh Air
65
215
cm
Gas Consumption Coefficient
Heat Consumption
Heat Consumption Coefficent
Gas Consumption
70
[ Sm3/h ]
75
220
152
210
183
96
5
5
27
672
645,1
66,7
0
C
g/m2
With Heat Recovery
µ%
Heat Efficiency
Exhaust Air "Absolute Humidity- Gas Consumption"
225
140
10
Stenter
Knitted 20/1 Single Jersey
meter
3
Sm /kg H2O
3
55
kcal/h
kcal/kg H2O
m3/h
0
C
%RH
kg/h
kcal/h
kcal/h
g H2O/kg dry air
kg/h
503525
781
9155
kg/h
4872
4872
Dry Bulb Temperature
kcal/h
0
C
-282469
149,21
-140567
35
Relative Humidity
Volumetric Fresh Air Need
Heat qexhaust Air
%RH
m3/h
kcal/h
1,09
6244
750759
90
4556
608856
Dry Bulb Temperature
Relative Humidity
Volumetric Flow Rate for Fresh Air
0
C
152,41
67,78
%RH
3
m /h
3,833
8350
68,745
6689
MASS BALANCE
ENERGIE BALANCE
Exhaust Air "Absolute Humidity - Flow Rate"
Heat Consumption
Recovery
kcal/h
15000
11000
Volumetric Flow
[m3/h]
10000
9000
8000
7000
6000
5000
4000
Mass Flow
[kg/h]
225
18
220
215
210
205
200
195
190
185
180
175
170
165
Exhaust Air Absolute Humidity
w [ g H2O/kg dry air ]
160
3000
2000
155
150
1000
kcal/h
Fırın iç ısıl gücü
450000
iç ısıl gücü yüzdesi cinsinde ısı kaybı
kcal
%
75164
10,4
Exhaust Air
450696,4
Dry Fabric
45024,0
45024,0
450696,4
400000
Heat Energy [kcal/h]
12000
[ xxxx/h ]
13000
0,0
0,0
with
Heat consumption with
theHeat
fabric
atık hava ile ısıl sarfiyat
500000
Exhaust Air Flow Rate
14000
570
35
90
610
-17593
7805
151
5481
350000
300000
250000
200000
150000
100000
50000
0
Seri 1
Heat Loss
7804,6
DGHS Direct Gas Heated Stenter
Exhaust Air "Absolute - Relative Humidity"
Exhaust Air Absolute Humidity-Gas Consumption
58,4
58,1
57,5
57,1
56,8
175 170 165 160
w [g H2O/kg dry air]
56,5
56,1
0,0967
0,1008
0,0973
0,1014
0,0984
0,1025
0,0990
0,1031
0,0996
0,1037
0,1001
0,1043
0,1007
0,1049
65
65,4
66,1
66,5
66,9
67,3
9155
9155
9155
9155
9155
9155
155
150
0,090
0,080
225
Without Heat
55,8
55,5 55,1
0,1013
0,1056
0,1019
0,1062
0,1025
0,1068
67,7
68,1
68,5
9155
9155
9155
220
215 210 205 200 195 190 185 180
Exhaust Air Absolute Humidity
Recovery
54,8 54,5
54,2
53,9
175 170 165 160
w [ g H2O/kg dry air ]
µ%
0,1031
0,1074
0,1037
0,1080
0,1043
0,1087
0,1049
0,1093
Sm /kg fabric
68,9
69,3
69,7
70,1
70,5
9155
9155
9155
9155
9155
Sm /h
3
kcal/Sm gas
kcal/h
kcal/kg H2O
m3/h
deg C
%RH
kg/h
kcal/h
kcal/h
g H2O/kg dry air
kg/h
595075
922
598737
928
605145
938
608807
944
612469
949
616132
955
619794
961
623456
966
627118
972
630780
978
634442
983
638104
989
641766
995
645428
1000
674
35
90
721
-20792
17852
220
3455
678
35
90
725
-20920
17962
212,8
3594
685
35
90
733
-21144
18154
203
3802
689
35
90
737
-21272
18264
197,6
3927
694
35
90
742
-21400
18374
192,8
4045
698
35
90
746
-21528
18484
188,4
4160
702
35
90
751
-21656
18594
184
4281
706
35
90
755
-21784
18704
179,9
4401
710
35
90
759
-21912
18814
175,96
4522
714
35
90
764
-22040
18923
172,3
4641
718
35
90
768
-22168
19033
169
4754
723
35
90
773
-22295
19143
166
4862
727
35
90
777
-22423
19253
163
4974
731
35
90
782
-22551
19363
160
5092
3
3
Sm /kg H2O
3
155
150
0,070
Heat Efficiency
Gas Consumption Coefficient
Gas Consumption
Gas Calorific Value
Heat Consumption
Heat Consumption Coefficient
Combustion Air
Dry Bulb Temperature
Relative Humidity
Combustion Air m1 fresh air
Heat q1 fresh air
Heat Losses
w Absolute Humidity
mexhaust air Exhaust Air
m2 Fresh air
Heat q2 Fresh air
2735
2869
3069
3189
3303
3413
3530
3646
3763
3878
3986
4089
4197
4310
kg/h
-78914
35
-82785
35
-88550
35
-92028
35
-95310
35
-98493
35
-101869
35
-105196
35
-108575
35
-111883
35
-115012
35
-117986
35
-121103
35
-124373
35
kcal/h
deg C
90
2557
631905
90
2683
639456
90
2870
651662
90
2982
658819
90
3089
665781
90
3192
672644
90
3301
679701
90
3409
686708
90
3519
693767
90
3626
700755
90
3727
707564
90
3824
714218
90
3925
721015
90
4031
727965
%RH
m3/h
kcal/h
Relative Humidity
Volumetric flow rate for Fresh Air
Heat qexhaust air
152,65
152,14
152,15
152,01
152,03
152,12
152,07
152,05
152,00
152,00
152,12
152,34
152,47
152,48
deg C
Dry Bulb Temperature
5,096
5737
5,039
5909
4,863
6177
4,782
6336
4,691
6489
4,598
6639
4,521
6794
4,445
6949
4,375
7105
4,304
7258
4,226
7406
4,142
7549
4,069
7696
4,008
7849
%RH
m3/h
Relative Humidity
Volumetric Flow Rate for Fresh Air
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
700.000
92080
19,4
90468
19,9
[ kcal/h]
600.000
Heat Energy
45024,0
541967,1
45024,0
545519,3
88194
20,6
86923
21,0
45024,0
549071,4
85774
21,4
45024,0
552623,6
84706
21,8
45024,0
556175,7
83631
22,2
45024,0
559727,8
82618
22,6
45024,0
563280,0
81635
23,0
45024,0
566832,1
45024,0
570384,3
80712
23,4
45024,0
45024,0
45024,0
Total Heat
Consumption581040,7
573936,4
577488,5
79870
23,8
79097
24,2Fabric
with
78321
24,6
Internal Energy of Stenter
HR-with Exhaust Air
HR-with Exhaust Air;
450696,4
400.000
HR-with Fabric
HR-with Heat Loss
300.000
HR-Total Heat Consumption
HR-Internal Energy of Stenter
200.000
600000
77541
25,0
500000
400000
300000
200000
100000
100.000
0
Heat Consumption
withhout Heat Recovery
Heat Loss
HR-Total Heat Consumption;
503525
500.000
with Exhaust Air
Heat Energy [kcal/h]
45024,0
535750,9
Dry Bulb Temperature
MASS BALANCE
ENERGY BALANCE
Exhaust Air "Absolute Humidity - Heat Consumption"
800.000
45024,0
532198,8
[ Sm3/kg ]
Sm3/kg fabric
Gas Consumption
[ RH% ]
0,100
Fresh Air for Burners
215 210 205 200 195 190 185 180
Exhaust Air Absolute Humidity
0,110
Fresh Air
220
Sm3/kg H2O
Exhaust Air
225
0,120
Exhaust Air Relative Humudity
Dry Fabric outlet
Humidity [RH%];
220; 5
12,0
11,5
11,0
10,5
10,0
9,5
9,0
8,5
8,0
7,5
7,0
6,5
6,0
5,5
5,0
4,5
4,0
3,5
3,0
2,5
2,0
1,5
1,0
0,5
0,0
150
155
160
165
170
175
180
185
190
195
200
205
210
Exhaust Air Absolute Humidity
w [ g H2O/kg dry air ]
215
220
225
0
Seri 1
Heat Loss
17852,3
Exhaust Air
532198,8
Dry Fabric
45024,0
19
PROSES ANALİZ 5
22
PROCESS ANALYSIS 5
DOKUMA KUMAŞ KURUTMA PROSESİ
DRYING PROCESS FOR WOVEN FABRIC
Z = altitude
Number of Chamber
Machine Type
Fabric Type
Chamber Temperature
Weight of Fabric
Width of Fabric
Squeezing Effect( Last Foulard)
Weight Variation
Dry Fabric Outlet Humudity
Production Speed
Production Capacity
Water Evoparation per Hour
Contact Time
Exhaust Air " Absolute Humidity - Heat Efficiency"
With Heat Recovery;
43,902; 12,1
10
9
8
Heat Efficiency
11
[%]
12
Fabric Inlet Temperature
Dry Fabric Outlet Temperature
Heat on the Wet Fabric
Heat on the Dry Fabric
7
52
52
51
51
50
50
49
49
48
48
47
47
46
46
45
E x h a u s t A i r A b s o l u t e H u m i d i t y w [ g H2O/kg dry air]
45
44
44
43
Without Heat Recovery
Recovered Heat
6
Heat Recovery
%
m/min
kg fabric/h
kg H2O/h
sec.
0
C
60
0
C
190
kcal/h
kcal/h
-8568
207366
kcal/h
kcal/h
592054
-273826
-46,25
45
40
with heat recovery;
43,902; 34,76
Gas Consumption
Gas Calorific Value
Sm /h
3
kcal/Sm gas
3
34,76
kcal/h
kcal/kg H2O
318228
4457
kg/h
360
35
90
368
-10975
32077
43,902
7888
3
Sm /kg H2O
43
Fresh Air for Burners
Combustion Air
Dry Bulb Temperature
Relative Humidity
Combustion Air m1 fresh air
Heat q1 fresh air
Machine Body Heat Losses
Absolute Humidity w
Exhaust Air mexhaust air
Fresh Air m2fresh air
30
9155
m3/h
0
C
%RH
kg/h
kcal/h
kcal/h
g H2O/kg dry air
kg/h
7520
7520
Dry Bulb Temperature
kcal/h
0
C
-497941
177
-224115
35
Relative Humidity
Volumetric Fresh Air Need
Heat qegzost air
%RH
3
m /h
kcal/h
0,54
10759
596268
90
7358
322442
Heat q2fresh air
Exhaust Air
44
35
12,1
0,0341
0,4868
3
Sm /kg fabric
Pre-Heated Fresh Air
50
[ Sm3/h ]
55
46
45
w [ g H 2O/kg dry air ]
%
%w
Gas Consumption Coefficient
Heat Consumption
Heat Consumption Coefficent
Gas Consumption
60
50
49
48
47
Exhaust Air Absolute Humidity
cm
%
65
51
190
200
180
7
0
0
47,2
1020
71,4
30,5
0
C
g/m2
With Heat Recovery
µ%
Heat Efficiency
Exhaust Air "Absolute Humidity- Gas Consumption"
52
500
8
Stenter
Woven 40/60 Cotton/Polyester
meter
0
C
190
56
%RH
3
m /h
0,502
11760
37,596
8365
Dry Bulb Temperature
Relative Humidity
Volumetric Flow Rate for Fresh Air
MASS BALANCE
ENERGIE BALANCE
Heat Consumption
With Heat Recovery
Exhaust Air "Absolute Humidity - Flow Rate"
12000
8000
7000
6000
5000
Mass Flow
[kg/h]
52
20
52
51
51
50
50
49
49
48
48
Exhaust Air Absolute Humidity
47
47
46
w [ g H2O/kg dry air ]
46
45
4000
45
44
3000
Fırın iç ısıl gücü
iç ısıl gücü yüzdesi cinsinde ısı kaybı
200.000
Heat Energy [kcal/h]
9000
[ xxxx/h ]
10000
Exhaust Air Flow Rate
11000
Volumetric Flow
[m3/h]
Heat consumption with the fabric
250.000
atık hava ile ısıl sarfiyat
kcal/h
kcal/h
kcal
%
0,0
0,0
198798,0
87352,8
33909
94,6
150.000
100.000
50.000
0
Seri 1
Heat Loss
32077,0
Exhaust Air
87352,8
Dry Fabric
198798,0
DGHS Direct Gas Heated Stenter
Exhaust Air "Absolute - Relative Humidity"
0,7
with heat recovery;
43,902; 0,502
0,6
0,5
0,4
0,3
0,2
52
52
51
51 50 50 49 49 48
Exhaust Air Absolute
8,3
8,2
8,0
7,8
48 47 47
Humidity
7,7
46 46 45 45
w [g H2O/kg dry air]
7,5
7,4
0,0495
0,7064
0,0505
0,7217
0,0516
0,7370
0,0527
0,7522
0,0537
0,7675
0,0548
0,7828
0,0559
0,7980
50,44
51,53
52,62
53,71
54,8
55,89
9155
9155
9155
9155
9155
9155
44
44
43
0,1
Sm3/kg fabric
52
Without Heat
7,2
7,1
7,0
0,0569
0,8133
0,0580
0,8286
0,0591
0,8438
56,98
58,07
59,16
9155
9155
9155
52
51
51
50
50
49
49
48
48
47
47
46
46
45
Exhaust Air Absolute Humidity
w [ g H2O/kg dry air ]
Recovery
6,9
6,7
6,6
6,5
µ%
0,0601
0,8591
0,0612
0,8744
0,0623
0,8896
0,0634
0,9057
Sm /kg fabric
60,25
61,34
62,43
63,52
64,67
9155
9155
9155
9155
9155
Sm /h
3
kcal/Sm gas
3
3
Sm /kg H2O
3
461778
6467
471757
6607
481736
6747
491715
6887
501694
7027
511673
7166
521652
7306
531631
7446
541610
7586
551589
7725
561568
7865
571547
8005
581526
8145
592054
8292
kcal/h
kcal/kg H2O
523
35
90
534
-15926
46547
51,715
4234
534
35
90
546
-16270
47553
50,855
4461
545
35
90
557
-16614
48559
50,09
4685
557
35
90
569
-16958
49564
49,383
4913
568
35
90
581
-17302
50570
48,744
5139
579
35
90
592
-17647
51576
48,16
5365
591
35
90
604
-17991
52582
47,616
5593
602
35
90
615
-18335
53588
47,12
5819
613
35
90
627
-18679
54594
46,66
6046
625
35
90
638
-19023
55600
46,235
6272
636
35
90
650
-19367
56605
45,84
6497
647
35
90
661
-19712
57611
45,47
6724
658
35
90
673
-20056
58617
45,123
6951
670
35
90
685
-20419
59678
44,781
7190
m /h
deg C
%RH
kg/h
kcal/h
kcal/h
g H2O/kg dry air
3
kg/h
45
44
Gas Consumption
Gas Calorific Value
Heat Consumption
Heat Consumption Coefficient
Combustion Air
Dry Bulb Temperature
Relative Humidity
Combustion Air m1 fresh air
Heat q1 fresh air
Heat Losses
w Absolute Humidity
mexhaust air Exhaust Air
m2 Fresh air
3699
3915
4128
4344
4559
4773
4990
5204
5419
5633
5847
6062
6278
6505
kg/h
-116686
35
-123016
35
-129465
35
-135856
35
-142232
35
-148701
35
-155095
35
-161507
35
-167889
35
-174264
35
-180666
35
-187091
35
-193862
35
kcal/h
deg C
Heat q2 Fresh air
90
3620
342609
90
3831
358363
90
4039
374010
90
4251
389776
90
4461
405484
90
4670
421177
90
4882
436964
90
5092
452675
90
5303
468404
90
5512
484104
90
5722
499795
90
5932
515515
90
6143
531257
90
6365
547858
%RH
3
m /h
kcal/h
Relative Humidity
Volumetric Flow Rate for Fresh Air
Heat qexhaust air
190
190
190
190
190
190
190
190
190
190
190
190
190
190
deg C
Dry Bulb Temperature
0,575
6721
0,566
7052
0,559
7386
0,552
7719
0,546
8051
0,541
8386
0,535
8718
0,531
9052
0,526
9384
0,522
9716
0,518
10049
0,514
10383
0,511
10734
%RH
3
m /h
Relative Humidity
Volumetric Flow Rate for Fresh Air
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
Exhaust
Air
"Absolute
Humidity
- Heat
Consumption"
198798,0
198798,0
198798,0
198798,0
198798,0
198798,0
198798,0
198798,0
35660
133,3
[ kcal/h]
35473
136,9
243352,7
252325,7
35294
140,4
35134
143,9
261298,8
34989
147,4
270271,9
279245,0
34850
150,9
34725
154,3
288218,1
297191,2
34609
157,7
306164,2
34502
161,1
34403
164,5
198798,0
315137,3
198798,0
324110,4
198798,0
333577,4
Total Heat Consumption
34310
34221
with Exhaust Air
167,9
171,3
with Fabric
Heat Loss
400.000
Internal Energy of Stenter
HR-Total Heat Consumption;
318228
300.000
HR-with Exhaust Air
HR-with Fabric
HR-with Heat Loss
200.000
HR-Total Heat Consumption
HR-Internal Energy of Stenter
0
Heat Consumption
without Heat Recovery
250.000
200.000
150.000
100.000
50.000
HR-with Exhaust Air; 87352,8
100.000
MASS BALANCE
ENERGY BALANCE
34134
174,8
Heat Energy [kcal/h]
35876
500.000
129,7
Heat Energy
Dry Bulb Temperature
0,583
6387
198798,0
234379,6
0
43
44
45
46
47
48
Exhaust Air Absolute Humidity
[ Sm3/kg ]
Heat Efficiency
Gas Consumption Coefficient
-110250
35
198798,0
600.000198798,0
216433,4
225406,5
Gas Consumption
0,8
Fresh Air for Burners
0,9
Fresh Air
1,0
0,950
0,900
0,850
0,800
0,750
0,700
0,650
0,600
0,550
0,500
0,450
0,400
0,350
0,300
0,250
0,200
0,150
0,100
0,050
0,000
Exhaust Air
1,1
Sm3/kg H2O
Exhaust Air Relative Humudity
1,2
[ RH% ]
Exhaust Air Absolute Humidity-Gas Consumption
1,3
49
50
w [ g H2O/kg dry air ]
51
52
Seri 1
Heat Loss
46546,8
Exhaust Air
216433,4
Dry Fabric
198798,0
21
PROSES ANALİZ 6
22
PROCESS ANALYSIS 6
DOKUMA KUMAŞ KURUTMA VE TERMOFİKSE PROSESİ
DRYING AND HEATSETTING PROCESS FOR WOVEN FABRIC
Z = altitude
Number of Chamber
Machine Type
Fabric Type
Chamber Temperature
Weight of Fabric
Width of Fabric
Squeezing Effect( Last Foulard)
Weight Variation
Dry Fabric Outlet Humudity
Production Speed
Production Capacity
Water Evoparation per Hour
Contact Time
Exhaust Air " Absolute Humidity - Heat Efficiency"
64
58
56
54
52
50
48
Heat Efficiency
60
[%]
With Heat Recovery; 111; 62
61,0
Wet Fabric Inlet Temp
Dry Fabric Outlet Temp
Heat on the Wet Fabric
Heat on the Dry Fabric
46
44
300
290
280
270
260
250 240 230 220 210 200 190 180 170 160 150
E x h a u s t A i r A b s o l u t e H u m i d i t y w [ g H2O/kg dry air]
140
130
120
110
Without Heat Recovery
Recovered Heat
42
Heat Recovery
Gas Consumption Coefficient
120
Gas Consumption
Gas Calorific Value
95
90
with heat recovery;
111; 81,66
270
260 250 240 230 220 210 200 190 180 170 160 150
Exhaust Air Absolute Humidity
w [ g H 2O/kg dry air ]
140
130
120
85
110
Absolute Humidity w
Exhaust Air mexhaust air
Fresh Air m2fresh air
Heat q2fresh air
80
Dry Bulb Temperature
Relative Humidity
Volumetric Fresh Air Need
Heat qEgzost Air
Exhaust Air
280
Fresh Air for Burners
100
Combustion Air
Dry Bulb Temperature
Relative Humidity
Combustion Air m1 fresh air
Heat q1 fresh air
Machine Body Heat Losses
Pre-Heated Fresh Air
105
Heat Consumption
Heat Consumption Coefficent
Gas Consumption
110
[ Sm3/h ]
115
290
150
200
180
70
0
4
60,1
1298
856,8
24,0
0
C
g/m2
cm
%
%
%w
m/min
kg fabric/h
kg H2O/h
sec.
0
C
60
0
C
120
kcal/h
kcal/h
-56859
172894
kcal/h
kcal/h
1061980
-305319
-28,75
%
With Heat Recovery
µ%
Heat Efficiency
Exhaust Air "Absolute Humidity- Gas Consumption"
300
500
8
Stenter
Woven 40/60 Cotton/Polyester
meter
Dry Bulb Temperature
Relative Humidity
Volumetric Flow Rate for Fresh Air
61,0
0,0637
0,0965
Sm3/kg fabric
3
Sm /kg H2O
Sm /h
3
kcal/Sm gas
3
82,65
kcal/h
kcal/kg H2O
m3/h
0
C
%RH
kg/h
kcal/h
kcal/h
g H2O/kg dry air
kg/h
kg/h
756661
883
857
35
90
876
-26096
47503
111
11251
10376
10376
kcal/h
0
C
-614540
150
1,06
13944
1233758
-309220
35
90
10153
928439
150
3,050
16864
56
88,294
13115
9155
%RH
m3/h
kcal/h
0
C
%RH
m3/h
MASS BALANCE
ENERGIE BALANCE
Heat Consumption
With Heat Recovery
Exhaust Air "Absolute Humidity - Flow Rate"
Heat consumption with the fabric
700.000 atık hava ile ısıl sarfiyat
18000
14000
13000
12000
11000
10000
9000
8000
7000
6000
Mass Flow
[kg/h]
5000
4000
300
22
290
280
270
260 250 240 230 220 210 200 190 180 170 160 150
Exhaust Air Absolute Humidity
w [ g H2O/kg dry air ]
140
130
120
110
3000
600.000
iç ısıl gücü yüzdesi cinsinde ısı kaybı
kcal
%
116034,9
593122,7
48929
97,1
500.000
Heat Energy [kcal/h]
15000
Volumetric Flow
[m3/h]
Fırın iç ısıl gücü
[ xxxx/h ]
16000
Exhaust Air Flow Rate
17000
kcal/h
kcal/h
0,0
0,0
400.000
300.000
200.000
100.000
0
Seri 1
Heat Loss
47503,2
Exhaust Air
593122,7
Dry Fabric
116034,9
DGHS Direct Gas Heated Stenter
Exhaust Air "Absolute - Relative Humidity"
Exhaust Air Absolute Humidity-Gas Consumption
4,0
3,5
3,0
with heat recovery;
111; 3,050
2,5
2,0
1,5
1,0
0,5
300 290 280 270 260 250 240 230 220 210 200 190 180 170 160 150 140 130 120 110
Exhaust Air Absolute Humidity
w [g H2O/kg dry air]
55,4
54,3
53,2
52,1
51,1
50,1
49,2
0,0702
0,1064
0,0716
0,1085
0,0731
0,1107
0,0746
0,1130
0,0760
0,1152
0,0775
0,1174
0,0790
0,1197
91,14
92,94
94,86
96,78
98,70
100,62
9155
9155
9155
9155
9155
9155
0,0
0,110
0,100
0,090
0,080
Sm3/kg fabric
Without Heat
48,3
47,4 46,6
0,0805
0,1219
0,0820
0,1242
0,0834
0,1264
102,54
104,46
106,38
9155
9155
9155
Recovery
45,8 45,0
44,3
43,5
µ%
0,0849
0,1286
0,0864
0,1310
0,0878
0,1331
0,0894
0,1354
Sm3/kg fabric
108,30
110,20
112,20
114,00
116,00
9155
9155
9155
9155
9155
Sm /h
3
kcal/Sm gas
3
Sm /kg H2O
3
850866
993
868443
1014
886021
1034
903599
1055
921176
1075
938754
1096
956331
1116
973909
1137
991487
1157
1008881
1178
1027191
1199
1043670
1218
1061980
1239
945
35
90
966
-28776
52383
292,5
3325
2360
963
35
90
985
-29345
53417
257,4
3850
2865
983
35
90
1005
-29951
54521
229,1
4411
3406
1003
35
90
1025
-30557
55624
207,2
4971
3946
1023
35
90
1046
-31163
56728
189,8
5529
4484
1043
35
90
1066
-31770
57831
175,5
6092
5026
1063
35
90
1086
-32376
58935
163,7
6650
5563
1083
35
90
1107
-32982
60038
153,65
7212
6105
1103
35
90
1127
-33588
61142
145,1
7771
6644
1123
35
90
1147
-34194
62246
137,7
8330
7183
1142
35
90
1168
-34794
63338
131,3
8883
7716
1163
35
90
1189
-35426
64487
125,35
9467
8279
1182
35
90
1208
-35994
65522
120,6
9992
8784
1203
35
90
1229
-36626
66671
115,85
10578
9349
kcal/h
kcal/kg H2O
m3/h
deg C
%RH
kg/h
kcal/h
kcal/h
g H2O/kg dry air
kg/h
kg/h
-70328
35
90
2309
765073
-85390
35
90
2804
796148
-101499
35
90
3333
829338
-117596
35
90
3861
862515
-133627
35
90
4387
895626
-149775
35
90
4918
928854
-165794
35
90
5444
961954
-181953
35
90
5974
995193
-198015
35
90
6501
1028335
-214073
35
90
7029
1061473
-229947
35
90
7550
1094250
-246721
35
90
8101
1128816
-261782
35
90
8595
1159889
-278613
35
90
9148
1194512
kcal/h
deg C
%RH
m3/h
kcal/h
150
6,406
6222
150
5,860
6927
150
5,392
7680
150
5,006
8433
150
4,680
9184
150
4,409
9938
150
4,171
10689
150
3,969
11444
150
3,789
12196
150
3,630
12947
150
3,489
13691
150
3,358
14475
150
3,251
15180
150
3,146
15967
deg C
%RH
m3/h
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
Exhaust
"Absolute
Humidity
- Heat
Consumption"
116034,9 Air
116034,9
116034,9
116034,9
116034,9
116034,9
116034,9
116034,9
76873
69,5
63,7
900.000
Heat Energy
[ kcal/h]
800.000
714361,6
72222
75,5
730835,7
68404
81,3
65223
87,0
747309,8
62507
92,5
763783,9
60189
97,9
780258,0
58161
103,2
796732,0
56393
108,4
813206,1
116034,9
846669,1
829508,6
54831
113,5
53455
118,5
116034,9
879274,0
Total Heat Consumption
52155
51102
with Exhaust Air
123,6
128,2
Heat Efficiency
Gas Consumption Coefficient
Gas Consumption
Gas Calorific Value
Heat Consumption
Heat Consumption Coefficient
Combustion Air
Dry Bulb Temperature
Relative Humidity
Combustion Air m1 fresh air
Heat q1 fresh air
Heat Losses
w Absolute Humidity
mexhaust air Exhaust Air
m2 Fresh air
Heat q2 Fresh air
Dry Bulb Temperature
Relative Humidity
Volumetric Flow Rate for Fresh Air
Heat qexhaust air
Dry Bulb Temperature
Relative Humidity
Volumetric Flow Rate for Fresh Air
MASS BALANCE
ENERGY BALANCE
Heat Consumption
Without Heat Recovery
700000
50035
600000
133,2
500000
Heat Loss
Internal Energy of Stenter
600.000
0,060
with Fabric
HR-Total Heat Consumption;
756661
700.000
HR-with Exhaust Air
HR-with Exhaust Air; 593122,7
HR-with Fabric
500.000
HR-with Heat Loss
400.000
HR-Total Heat Consumption
300.000
HR-Internal Energy of Stenter
200.000
400000
300000
200000
100000
100.000
0
116034,9
862113,5
Heat Energy [kcal/h]
1.000.000
82243
116034,9
697887,6
0,070
300 290 280 270 260 250 240 230 220 210 200 190 180 170 160 150 140 130 120 110
Exhaust Air Absolute Humidity
w [ g H2O/kg dry air ]
834387
974
116034,9
116034,9
1.100.000681413,5
665969,0
[ Sm3/kg ]
0,120
Gas Consumption
4,5
Fresh Air for Burners
5,0
0,130
Sm3/kg H2O
Fresh Air
5,5
Exhaust Air
6,0
0,140
[ RH% ]
6,5
Exhaust Air Relative Humudity
7,0
0
110
120
130
140
150 160 170 180 190 200 210 220 230 240 250 260
Exhaust Air Absolute Humidity
w [ g H 2O/kg dry air ]
270
280
290
300
Seri 1
Heat Loss
52382,8
Exhaust Air
665969,0
Dry Fabric
116034,9
23
PROSES ANALİZ 7
22
PROCESS ANALYSIS 7
DOKUMA KUMAŞ KURUTMA VE TERMOFİKSE PROSESİ
DRYING AND HEATSETTING PROCESS FOR WOVEN FABRIC
Z = altitude
Number of Chamber
Machine Type
Fabric Type
Chamber Temperature
Weight of Fabric
Width of Fabric
Squeezing Effect( Last Foulard)
Weight Variation
Dry Fabric Outlet Humudity
Production Speed
Production Capacity
Water Evoparation per Hour
Contact Time
110
105
100
95
90
85
80
E x h a u s t A i r A b s o l u t e H u m i d i t y w [ g H2O/kg dry air]
75
70
42
41
40
39
38
37
36
35
34
33
32
31
30
29
28
27
26
25
Heat Efficiency
With Heat Recovery; 72,8;
40,6
[%]
Exhaust Air " Absolute Humidity - Heat Efficiency"
Wet Fabric Inlet Temperature
Dry Fabric Outlet Temperature
Heat on the Wet Fabric
Heat on the Dry Fabric
Without Heat Recovery
Recovered Heat
Heat Recovery
91
%
m/min
kg fabric/h
kg H2O/h
sec.
0
C
60
0
C
190
kcal/h
kcal/h
-26103
114865
kcal/h
kcal/h
824957
-299249
-36,27
71
66
Gas Consumption
Gas Calorific Value
Sm /h
3
kcal/Sm gas
3
57,423
kcal/h
kcal/kg H2O
525708
1329
kg/h
595
35
90
608
-18131
54521
72,8
10422
75
61
70
[ Sm3/h ]
3
Sm /kg H2O
fresh air for burners
Combustion Air
Dry Bulb Temperature
Relative Humidity
Combustion Air m1 fresh air
Heat q1 fresh air
Machine Body Heat Losses
Absolute Humidity w
Exhaust Air mexhaust air
Fresh Air m2fresh air
56
9155
m3/h
0
C
%RH
kg/h
kcal/h
kcal/h
g H2O/kg dry air
kg/h
9813
9813
Dry Bulb Temperature
kcal/h
0
C
-591711
154
-292462
35
Relative Humidity
Volumetric Fresh Air Need
Heat qegzost air
%RH
3
m /h
kcal/h
0,95
13318
992267
90
9602
693017
Heat q2fresh air
Exhaust air
with heat recovery;
72,8; 57,423
40,6
0,1016
0,1452
3
Sm /kg fabric
pre-heated fresh air
76
85
80
w [ g H 2O/kg dry air ]
%
%w
%
Heat Consumption
Heat Consumption Coefficent
Gas Consumption
81
100
95
90
Exhaust Air Absolute Humidity
cm
Gas Consumption Coefficient
86
105
190
200
180
70
0
0
26,2
565
395,5
55,0
0
C
g/m2
With Heat Recovery
µ%
Heat Efficiency
Exhaust Air "Absolute Humidity- Gas Consumption"
110
500
8
Stenter
Woven 40/60 Cotton/Polyester
meter
0
C
190
84
%RH
3
m /h
0,800
16207
17,767
12513
Dry Bulb Temperature
Relative Humidity
Volumetric flow rate for Fresh Air
MASS BALANCE
ENERGIE BALANCE
Heat Consumption
With Heat Recovery
Exhaust Air "Absolute Humidity - Flow Rate"
17000
13000
12000
11000
10000
9000
8000
Mass Flow
[kg/h]
7000
6000
110
24
105
100
95
90
Exhaust Air Absolute Humidity
85
80
w [ g H2O/kg dry air ]
75
70
5000
450.000
Fırın iç ısıl gücü
iç ısıl gücü yüzdesi cinsinde ısı kaybı
400.000
Heat Energy [kcal/h]
14000
[ xxxx/h ]
15000
Volumetric Flow
[m3/h]
Exhaust Air Flow Rate
16000
Heat consumption with the fabric
500.000
atık hava ile ısıl sarfiyat
kcal/h
kcal/h
kcal
%
0,0
0,0
88761,5
382424,9
40948
133,1
350.000
300.000
250.000
200.000
150.000
100.000
50.000
0
Seri 1
Heat Loss
54521,1
Exhaust Air
382424,9
Dry Fabric
88761,5
DGHS Direct Gas Heated Stenter
Exhaust Air "Absolute - Relative Humidity"
Exhaust Air Absolute Humidity-Gas Consumption
0,4
0,2
110
105
33,1
100
95
Exhaust Air Absolute
32,4
31,8
31,1
90
85
80
75
Humidity
w [g H2O/kg dry air]
30,5
29,9
29,3
0,1244
0,1777
0,1271
0,1816
0,1298
0,1854
0,1325
0,1893
0,1352
0,1931
0,1379
0,1970
0,1406
0,2009
70,288
71,813
73,338
74,863
76,388
77,913
9155
9155
9155
9155
9155
9155
70
0,0
[ RH% ]
0,190
0,180
0,170
0,160
0,150
0,140
Sm3/kg fabric
0,130
0,120
0,110
110
Without Heat
28,8
28,2 27,7
0,1433
0,2047
0,1460
0,2086
0,1487
0,2124
79,438
80,963
82,488
9155
9155
9155
105
100
95
90
85
80
75
Exhaust Air Absolute Humidity
w [ g H2O/kg dry air ]
Recovery
27,2 26,8
26,3
25,8
µ%
0,1514
0,2163
0,1541
0,2201
0,1568
0,2240
0,1595
0,2278
Sm /kg fabric
84,013
85,538
87,063
88,588
90,11
9155
9155
9155
9155
9155
Sm /h
3
kcal/Sm gas
3
3
Sm /kg H2O
3
643487
1627
657448
1662
671409
1698
685371
1733
699332
1768
713294
1804
727255
1839
741216
1874
755178
1909
769139
1945
783100
1980
797062
2015
811023
2051
824957
2086
kcal/h
kcal/kg H2O
729
35
90
745
-22193
66736
106,47
5522
744
35
90
761
-22674
68184
102,6
5838
760
35
90
777
-23156
69632
99,12
6154
776
35
90
793
-23637
71080
96
6468
792
35
90
809
-24119
72528
93,15
6784
808
35
90
825
-24600
73976
90,55
7101
824
35
90
842
-25082
75424
88,18
7416
839
35
90
858
-25563
76872
86
7732
855
35
90
874
-26045
78319
84
8047
871
35
90
890
-26526
79767
82,14
8363
887
35
90
906
-27008
81215
80,42
8679
903
35
90
922
-27489
82663
78,82
8995
918
35
90
939
-27971
84111
77,33
9310
934
35
90
955
-28451
85556
75,94
9625
m /h
deg C
%RH
kg/h
kcal/h
kcal/h
g H2O/kg dry air
3
kg/h
70
0,100
Heat Efficiency
Gas Consumption Coefficient
Gas Consumption
Gas Calorific Value
Heat Consumption
Heat Consumption Coefficient
Combustion Air
Dry Bulb Temperature
Relative Humidity
Combustion Air m1 fresh air
Heat q1 fresh air
Heat Losses
w Absolute Humidity
mexhaust air Exhaust Air
m2 Fresh air
4778
5077
5377
5675
5975
6275
6575
6875
7173
7473
7773
8073
8372
8671
kg/h
-142383
35
-151302
35
-160241
35
-169117
35
-178058
35
-187014
35
-195937
35
-204875
35
-213771
35
-222722
35
-231648
35
-240579
35
-249500
35
-258406
35
kcal/h
deg C
Heat q2 Fresh air
90
4675
652564
90
4968
674479
90
5261
696412
90
5553
718283
90
5846
740220
90
6140
762170
90
6433
784088
90
6727
806022
90
7019
827912
90
7313
849858
90
7606
871779
90
7899
893705
90
8192
915621
90
8484
937496
%RH
3
m /h
kcal/h
Relative Humidity
Volumetric Flow Rate for Fresh Air
Heat qexhaust air
190,01
190,02
190,01
190,05
190,03
190,01
190,02
190,01
190,03
190,01
190,01
190,01
190,01
190,01
deg C
Dry Bulb Temperature
1,111
9007
1,076
9471
1,045
9936
1,016
10399
0,990
10863
0,966
11329
0,944
11793
0,924
12258
0,904
12721
0,887
13186
0,870
13650
0,855
14115
0,841
14579
0,827
15042
%RH
3
m /h
Relative Humidity
Volumetric Flow Rate for Fresh Air
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
800.000
48453
47627
143,2
137,7
Heat Energy
[ kcal/h]
700.000
Exhaust
Air
"Absolute
Humidity
- Heat
Consumption"
88761,5
88761,5
88761,5
88761,5
88761,5
88761,5
88761,5
88761,5
88761,5
513016,0
46876
148,5
525529,5
46197
153,9
538042,9
45571
159,2
550556,3
44995
164,4
563069,8
575583,2
44467
169,6
43978
174,8
588096,7
600610,1
43528
179,9
613123,5
43106
185,1
42713
190,1
88761,5
625637,0
88761,5
650639,3
Total Heat Consumption
42347
42004
with Exhaust Air
195,2
200,2
with Fabric
Heat Loss
600.000
Internal Energy of Stenter
HR-Total Heat Consumption;
525708
500.000
400.000
HR-with Exhaust Air
HR-with Fabric
HR-with Exhaust Air;
382424,9
300.000
HR-with Heat Loss
HR-Total Heat Consumption
HR-Internal Energy of Stenter
200.000
Dry Bulb Temperature
MASS BALANCE
ENERGY BALANCE
Heat Consumption
without Heat Recovery
500.000
450.000
41683
205,3
400.000
350.000
300.000
250.000
200.000
150.000
100.000
100.000
0
88761,5
638150,4
Heat Energy [kcal/h]
88761,5
900.00088761,5
487989,1
500502,6
[ Sm3/kg ]
0,200
Gas Consumption
0,6
0,210
Fresh Air for Burners
with heat recovery;
72,8; 0,800
0,220
Sm3/kg H2O
Fresh Air
0,8
0,230
Exhaust Air
1,0
0,240
Exhaust Air Relative Humudity
1,2
50.000
0
70
75
80
85
90
Exhaust Air Absolute Humidity
95
100
w [ g H2O/kg dry air ]
105
110
Seri 1
Heat Loss
66736,0
Exhaust Air
487989,1
Dry Fabric
88761,5
25
PROSES ANALİZ 8
22
PROCESS ANALYSIS 8
DOKUMA KUMAŞ TERMOFİKSE PROSESİ
HEATSETTING PROCESS FOR WOVEN FABRIC
Z = altitude
Number of Chamber
Machine Type
Fabric Type
Chamber Temperature
Weight of Fabric
Width of Fabric
Squeezing Effect( Last Foulard)
Weight Variation
Dry Fabric Outlet Humudity
Production Speed
Production Capacity
Water Evoparation per Hour
Contact Time
125
120
115
110
105
100
95
90
E x h a u s t A i r A b s o l u t e H u m i d i t y w [ g H2O/kg dry air]
85
80
75
45
44
43
42
41
40
39
38
37
36
35
34
33
32
31
30
29
28
27
26
25
Heat Efficiency
With Heat Recovery; 78,9;
44,5
[%]
Exhaust Air " Absolute Humidity - Heat Efficiency"
Wet Fabric Inlet Temperature
Dry Fabric Outlet Temperature
Heat on the Wet Fabric
Heat on the Dry Fabric
Without Heat Recovery
Recovered Heat
Heat Recovery
kg fabric/h
kg H2O/h
sec.
0
C
60
0
C
190
kcal/h
kcal/h
-30353
133568
kcal/h
kcal/h
886204
-329035
-37,13
75
70
with heat recovery;
78,9; 60,8595
[ Sm3/h ]
65
75
Absolute Humidity w
Exhaust Air mexhaust air
Fresh Air m2fresh air
Heat q2fresh air
60
Dry Bulb Temperature
Relative Humidity
Volumetric Fresh Air Need
Heat qegzost air
Exhaust Air
80
Fresh Air for Burners
80
44,5
0,0926
0,1323
Sm /kg H2O
Combustion Air
Dry Bulb Temperature
Relative Humidity
Combustion Air m1 fresh air
Heat q1 fresh air
Machine Body Heat Losses
Pre-Heated Fresh Air
85
95
90
85
w [ g H 2O/kg dry air ]
%
m/min
3
Heat Consumption
Heat Consumption Coefficent
Gas Consumption
90
110
105
100
Exhaust Air Absolute Humidity
%
%w
Sm3/kg fabric
Gas Consumption
Gas Calorific Value
95
115
cm
%
Gas Consumption Coefficient
100
120
190
200
180
70
0
0
30,4
657
459,9
47,4
0
C
g/m2
With Heat Recovery
µ%
Heat Efficiency
Exhaust Air "Absolute Humidity- Gas Consumption"
125
500
8
Stenter
Woven 40/60 Cotton/Polyester
meter
Sm3/h
3
kcal/Sm gas
60,8595
kcal/h
kcal/kg H2O
m3/h
0
C
%RH
kg/h
kcal/h
kcal/h
g H2O/kg dry air
kg/h
kg/h
557169
1211
631
35
90
645
-19216
56162
78,9
10441
9796
9796
kcal/h
0
C
-620971
166
0,70
13671
1037979
-291936
35
90
9585
708944
190,0
0,855
16386
75
27,469
12328
9155
%RH
m3/h
kcal/h
Dry Bulb Temperature
Relative Humidity
Volumetric Flow Rate for Fresh Air
0
C
%RH
m3/h
MASS BALANCE
ENERGIE BALANCE
Heat Consumption
With Heat Recovery
Exhaust Air "Absolute Humidity - Flow Rate"
18000
14000
13000
12000
11000
10000
9000
8000
Mass Flow
[kg/h]
7000
6000
5000
125
26
120
115
110
105
100
95
90
85
Exhaust Air Absolute Humidity
w [ g H2O/kg dry air ]
80
75
4000
Fırın iç ısıl gücü
iç ısıl gücü yüzdesi cinsinde ısı kaybı
500.000
Heat Energy [kcal/h]
15000
[ xxxx/h ]
16000
Volumetric Flow
[m3/h]
Exhaust Air Flow Rate
17000
Heat consumption with the fabric
600.000
atık hava ile ısıl sarfiyat
kcal/h
kcal/h
kcal
%
0,0
0,0
103214,7
397792,0
42366
132,6
400.000
300.000
200.000
100.000
0
Seri 1
Heat Loss
56162,1
Exhaust Air
397792,0
Dry Fabric
103214,7
DGHS Direct Gas Heated Stenter
Exhaust Air "Absolute - Relative Humidity"
Exhaust Air Absolute Humidity-Gas Consumption
0,2
125
120
115
110
105
Exhaust Air Absolute
35,9
35,1
34,4
100
95
Humidity
33,7
33,0
90
85
w [g H2O/kg dry air]
32,4
31,7
0,1149
0,1642
0,1174
0,1677
0,1199
0,1713
0,1224
0,1748
0,1249
0,1784
0,1274
0,1820
0,1299
0,1855
75,5089
77,13
78,77
80,41
82,05
83,69
9155
9155
9155
9155
9155
9155
80
75
0,0
[ RH% ]
0,190
0,180
0,170
0,160
0,150
0,110
125
Without Heat
31,1
30,6 30,0
0,1324
0,1891
0,1349
0,1927
0,1374
0,1962
85,33
86,97
88,61
9155
9155
9155
120
115
110
105
100
95
Exhaust Air Absolute Humidity
Recovery
29,5 29,0
28,5
28,0
90
85
w [ g H2O/kg dry air ]
µ%
0,1399
0,1998
0,1424
0,2034
0,1449
0,2069
0,1473
0,2105
Sm3/kg fabric
90,25
91,89
93,53
95,17
96,8
9155
9155
9155
9155
9155
Sm3/h
3
kcal/sm gas
3
Sm /kg H2O
721139
1568
736154
1601
751168
1633
766182
1666
781196
1699
796210
1731
811225
1764
826239
1797
841253
1829
856267
1862
871281
1895
886204
1927
783
35
90
800
-23841
69681
123,6
5182
4382
800
35
90
817
-24353
71177
118,15
5521
4704
817
35
90
835
-24871
72690
113,31
5862
5027
834
35
90
852
-25388
74204
109
6202
5350
851
35
90
869
-25906
75717
105,15
6542
5673
868
35
90
887
-26424
77230
101,67
6883
5996
885
35
90
904
-26942
78744
98,54
7221
6317
902
35
90
921
-27460
80257
95,65
7564
6643
919
35
90
939
-27978
81771
93,05
7902
6963
936
35
90
956
-28495
83284
90,64
8244
7287
953
35
90
974
-29013
84797
88,41
8587
7613
970
35
90
991
-29531
86311
86,37
8927
7936
987
35
90
1008
-30049
87824
84,48
9267
8258
1003
35
90
1026
-30563
89328
82,73
9605
8580
kcal/h
kcal/kg H2O
m3/h
deg C
%RH
kg/h
kcal/h
kcal/h
g H2O/kg dry air
kg/h
kg/h
-130594
35
90
4288
672824
-140187
35
90
4603
696273
-149819
35
90
4919
719924
-159455
35
90
5235
743579
-169060
35
90
5551
767203
-178697
35
90
5867
790858
-188259
35
90
6181
814439
-197971
35
90
6500
838169
-207524
35
90
6814
861741
-217179
35
90
7131
885415
-226890
35
90
7450
909144
-236506
35
90
7765
932778
-246119
35
90
8081
956410
-255698
35
90
8395
979923
kcal/h
deg C
%RH
m3/h
kcal/h
190,06
1,259
8652
190,00
1,214
9149
190,00
1,172
9650
190,00
1,134
10151
190,02
1,099
10651
190,01
1,068
11152
190,06
1,039
11651
190,01
1,013
12155
190,06
0,988
12653
190,04
0,966
13155
190,00
0,946
13658
190,01
0,927
14158
190,02
0,909
14659
190,01
0,892
15157
deg C
%RH
m3/h
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
0,0
50895
139,8
134,0
[ kcal/h]
700.000
Heat Energy
Exhaust
Air
"Absolute
Humidity
- Heat
Consumption"
103214,7
103214,7
103214,7
103214,7
103214,7
103214,7
103214,7
103214,7
558735,3
49893
145,7
572236,1
48989
151,5
48172
157,2
585736,9
47427
162,8
599237,7
46751
168,4
612738,4
46120
174,0
626239,2
45549
179,5
639740,0
45016
185,0
653240,8
44518
190,5
103214,7
666741,6
103214,7
693660,8
Total Heat Consumption
44062
43636
with Exhaust Air
195,9
201,3
with Fabric
Heat Loss
600.000
HR-Total Heat Consumption;
557169
500.000
Internal Energy of Stenter
HR-with Exhaust Air
HR-with Fabric
HR-with Exhaust Air;
397792,0
400.000
HR-with Heat Loss
300.000
HR-Total Heat Consumption
HR-Internal Energy of Stenter
200.000
80
75
0,100
Heat Efficiency
Gas Consumption Coefficient
Gas Consumption
Gas Calorific Value
Heat Consumption
Heat Consumption Coefficient
Combustion Air
Dry Bulb Temperature
Relative Humidity
Combustion Air m1 fresh air
Heat q1 fresh air
Heat Losses
w Absolute Humidity
mexhaust air Exhaust Air
m2 Fresh air
Heat q2 Fresh air
Dry Bulb Temperature
Relative Humidity
Volumetric Flow Rate for Fresh Air
Heat qexhaust air
Dry Bulb Temperature
Relative Humidity
Volumetric Flow Rate for Fresh Air
MASS BALANCE
ENERGY BALANCE
Heat Consumption
without Heat Recovery
600.000
43240
206,6
500.000
400.000
300.000
200.000
100.000
100.000
0
103214,7
680242,4
Heat Energy [kcal/h]
800.000
52009
0,130
0,120
706125
1535
103214,7
545234,5
0,140
Sm3/kg fabric
691284
1503
103214,7
900.000103214,7
518388,5
531733,7
[ Sm3/kg ]
0,200
Gas Consumption
0,4
0,210
Fresh Air for Burners
0,6
0,220
Sm3/kg H2O
Fresh Air
0,8
0,230
Exhaust Air
1,0
with heat recovery;
78,9; 0,855
0,240
Exhaust Air Relative Humudity
1,2
0
75
80
85
90
95
100
105
110
115
Exhaust Air Absolute Humidity
w [ g H2O/kg dry air ]
120
125
Seri 1
Heat Loss
69680,7
Exhaust Air
518388,5
Dry Fabric
103214,7
27
DİZAYN VARYASYONLARI
VARIATIONS IN DESIGN
Örgü Hattı; Çapraz Hava Sirkülasyonlu, Dik veya Yatık tip zincir sistemi
Knitted Line; Counter Type Air Circulation System, Vertical or Horizontal Chain System
Örgü Hattı; Tek Taraftan Hava Sirkülasyonlu , Dik veya Yatık tip zincir sistemi
Knitted Line; One Sided Air Circulation, Vertical or Horizontal Chain System
Dokuma Hattı; Tek taraflı sirkülasyon veya Çapraz akım sirkülasyonlu üretilir, Yatık tip ray ve zincir sistemi
Woven Line; One Sided or Counter Type Air Circulation, Horizontal Chain System
Denim Hattı; Tek taraflı sirkülasyon veya Çapraz akım sirkülasyonlu üretilir, Yatık tip ray ve zincir sistemi
Denim Line; One Sided or Counter Type Air Circulation, Horizontal Chain System
28
22
DİZAYN VARYASYONLARI
VARIATIONS IN DESIGN
22
29
TEKNİK VERİLER
22
TECHNICAL DATAS
Makine çıkış sistemi
Exit System
3,5 m uzunluğunda zincir çıkış sistemi.
Kumaş çıkış çekici silindiri.
Anti statik elektrik giderici ünite.
Temaslı tip kumaş çıkış nem ölçme sistemi (opsiyonel).
Hava soğutma sistemi
Exit system with 3,5 m chain length
Fabric exit pulling roller
Antistatic electricity removal device
Fabric humidity measurement device (optional)
Air Cooling System
2,4 m uzunluğunda, 1x11 kW fanlı havalı tip çıkış kumaş
soğutma ünitesi.
Dokuma kumaşlar için kullanılan yüzey temaslı silindirli tip
soğutma.
2,4 m length, 1x7,5 kw blower fan, exit air cooling device
Water cooling tower for woven and denim fabric
Plaiting System
Plaiting on a trolley or A frame
Sallama (pastallama) sistemi
Big Batch Winding System with Peripherical Drive and
Plaiting System
Arabaya veya sıpaya pastallama sistemi
Üstten baskılı Dog Sarma Sistemi
Big Batcher Winding System with Centeral Drive (optional)
Göbekten tahrikli dog sarma sistemi (opsiyonel)
Üstten baskılı dok sarma ve
sallama sistemi
Big Batch Winding System with
Peripherical Drive and Plaiting
System
30
Su soğutma silindirleri
Water Cooling Cylinders
Çıkış sallama sistemi
Plaiting System
Kız Kulesi / İstanbul
AMERİKA
YUNANİSTAN
BANGLADEŞ
EKVATOR
BELARUS
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PERU
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PORTEKİZ
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31
İHTİYAÇLARINIZI
BİLİYORUZ
SİZİN İÇİN
ÜRETİYORUZ
DMS DİLMENLER MAKİNE VE TEKSTİL SAN. TİC. A.Ş.
Merkez / Head Quarter
Çobançeşme Mh. Mithatpaşa Cd. Çalışlar Sk. No:5 Kat:5 34196
Bahçelievler / İstanbul / Türkiye
Phone: +90 212 551 18 27
Fax : +90 212 551 11 62
Fabrika / Factory
Ergene 1 OSB Vakıflar Mh. E5 Yolu Üzeri Fabrikalar Sk. No:11 Ergene / Tekirdağ / Türkiye
Phone: +90 282 672 25 07
Fax : +90 282 672 22 63
[email protected] | www.dilmenler.com.tr
WE KNOW
YOUR NEEDS
AND PRODUCE
FOR YOU