OBEM SpA – Biella - Italy produces Fully Robotized Dyeing ... Conference Presentations... · OBEM...
Transcript of OBEM SpA – Biella - Italy produces Fully Robotized Dyeing ... Conference Presentations... · OBEM...
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May 9, 2012 AQUAFIT End Congress 1
May 9, 2012 AQUAFIT End Congress 2
OBEM SpA – Biella - Italyproduces
Fully Robotized Dyeing Plantsfor Fiber – Yarn - Fabric
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OBEM Previous AOP Experience
DYEING MACHINE
BIOFLOTATOR
WATER RECOVERY TANK
pH, TEMPERATURE, OXIGEN PEROXIDE
CONTROL
pH, TEMPERATURE,
CONTROL
DYEING
LIQUOR
WASHING
WATER
DECOLORED
WATER
DEPURATED
WATER DRAIN
REUSE OF DEPURATED
WATER
AOP REACTOR
ADVANCED OXIDATION
PROCESS AND
BIOTREATMENTS FOR WATER
RECYCLING IN TEXTILE
INDUSTRY
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Notes on OBEM Previous AOP Experience
ADOPBIO Project (Sixth Framework Programme)
� TRIPLE CELLS AOP reactors combined with BIOFLOTATION
Single AOP Cell Features
• 800 W conventional Medium Pressure lamp
• Horizontal mounting
• Triple internal flow
• Forced air lamp cooling
Total installed UV power: 2400 W
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AquaFit - New OBEM Approach
for Better Results & Cost Reduction
� Power reduction
� Increasing Efficiency
� Liquor Flow Optimisation
� New Combination of Processes from Advanced Partners
Reduction of
Total Process Cost
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AquaFit New Approach
for Better Results & Cost Reduction
Fresh water
Softening
Coolingwater
Te
xti
le f
inis
hin
g
pro
ce
ss
es
Concentrated
WW from
pre-treatment,
dyeing, printing,
finishing
Non-
concentrated
WW from
washing, rinsing Membrane NF/RO
Evapoconcentration/ controled crystallization
*AOP
Water for reuse Concen-trate
Heat recuperation
heat
*AOP = H2O2 / UV; H2O2 /O3; H2O2 / US; …
Incinerationor use in other
domains
possible path
Prefiltration
Processwater
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Processes schema
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AquaFit New Approach
for Better Results & Cost Reduction
Filtration technology
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End Users
Concentration technology
AOP reactor
Partners Involvement
New AOP Block Diagram
Storage tank 1000 liters
SandFilter
PreTreatment
TankAOP
TreatedWater
RecoveryTank
H2O2 H2SO4 NaOH
Reuse of depuratedwater or to following
process
pH
ORP
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New AOP Main Features
• Capacity : approx 100 to 150 liters/hour
• Power comsumption: approx 9 to 18 kWh per cu.m
• UV lamps: 1.44 kW LP Amalgam type
• Mixing device, pH and Redox control
• Circulating pump with flow control
• Batch or continuous working
• 1000 liters storage tank
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New AOP Design
• Main features
•Minimum gap between lamps (19 mm) and
between lamps and inner reactor surface (10 mm)
•Reduced section (92 x 182 mm )
•Chamber height closed to lamp height (1570 mm)
•Reduced volume (approx 20 liters)
•Cooling jacket
•Vertical mounting
The small gap between lamps assure a good UV
activity also with dense dyeing waste
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New OBEM AOP 3D View
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Usually Textile wastewaters have different properties
- Strongly Acidic - Strongly Alkaline
Proper Pretreatment
Process Combination(nanofiltration, ultrafiltration, bioflotation,
evapoconcentration, ecc.)
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It will be Necessary to Work on:Cost of Process to be Economically Sustainable
Variability of Cost of the Water versus Cost of Process
Adaptability of Process to the Requirements of National Regulation in force in various Countries
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ECOTINT
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Processes of textile dyeing with supercritical CO2
Partners involved:- OBEM spa- Filatura di Chiavazza- Filatura di Grignasco- Filtex - Como- Tintoria Vago- ENEA- Politecnico di Torino
MIUR
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ECOTINT
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Processes of textile dyeing with Supercritical CO2
Started in 1998 – Ended in 2001More than 50 tests on polyester, silk, wool and cotton yarnRated disperse and acid dyes
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ADOPBIO
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Advanced Oxidation Processes and Biotreatments for Water Recycling in the Textile Industry
Partners Involved:Stazione Sperimentale Seta (It)Univers. Of Maribor (Sl)Ecologia Applicata (It)Helios Italquartz (It)Robert Blondel (Fr)Dama Engineering (Sl)OBEM (It)TSP (Sl)
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ADOPBIO
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Advanced Oxidation Processes and Biotreatments for Water Recycling in the Textile Industry
Started in 2004 – Ended in 2007Manufactured a dyeing machine intefaced with the AOP reactor and the Bioflotation reactorTested different combination of AOP + Bioflotation treatmentsTested different wastewater of End Usersstandard production
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INTEXUSA
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Optimisation of dyeing processes with UltraSonic Technology and its integration with automatic on-line control
Partners Involved:ENEAPolitecnico di TorinoFLAINOXOBEMFinissaggio di TriveroITTTintoria Ferraris
POR-FESR 2007-2013
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INTEXUSA
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Optimisation of dyeing processes with UltraSonic Technology and its integration with automatic on-line control
Started in 2009 – Ended in 2011
Manufactured one lab US dyeing machine and three industrial scale device for US dyeing of yarn, pantyhose, garnment, fabric.Carried out more than 50 tests on wool, cotton, polyester, acrilic, viscose
POR-FESR 2007-2013
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STARTES
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Developement of an advanced dyeing system of weaving yarn in bobbins whith online monitoring system and its integration into the production chain
Partners involved
Lanificio F.lli CerrutiOBEMFARBOTEX
POR-FESR 2007-2013POLI DI INNOVAZIONE
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STARTES
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Developement of an Advanced DyeingSystem on Packages of Yarn for Weaving with online monitoringsystem and its integration into the production chain
Started in 2011 …. Work in progress.
Test on dyestuff and chemicalsOptimization of dyeing parametersOptimization of liquor flow and material holders
POR-FESR 2007-2013POLI DI INNOVAZIONE
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Universities and Research Institutes
Politecnico di Torino- Ecotint - Intexusa
ENEA- Ecotint - Intexusa
University of Maribor- Adopbio – Aquafit
Stazione Seta- Adopbio
OBEM Collaboration Experience with
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A ….green ….Thank You
for Your Kind Attention!
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Spare Slides
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Previous OBEM AOP Experience
� ADOPBIO SYSTEM REACTORS
Dyeing waste drains too dense:the UV light is completely absorbedin few mm of thickness of waste water.
No UV rays can penetrate in externalreactor chambers
Low reactor efficiency
Real flow capacity approx 15-20 l/h
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Previous OBEM AOP Experience
ADOPBIO Project (Sixth Framework Programme)
� TRIPLE CELLS AOP reactors combined with BIOFLOTATION
Single AOP Cell Features
• 800 W conventional Medium Pressure lamp
• Horizontal mounting
• Triple internal flow
• Forced air lamp cooling
Total installed UV power: 2400 W
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Type of UV Lamps of New OBEM AOP
� Lamp type: GPHA1554T6L (Amalgam)
� Lamp power : 240 W
� Lamp quantity: 6
� Total power: 1440 W
� Ballast: electronic
� Power control: 70 to 100 %
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Comparison of UV Lamps Between 2 AOPs
Output wavelenght: 254 nm
UV emission: approx 400-500 % than
conventional UV lamp
Operating life extended to over
12000 hours
Operating temperature lower than
100 °C (No cooling required)
Low pressure Amalgam (New AOP)
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AOP Diagram
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AOP Working Diagram
WORKING MODE 1BATCH FROM TANK 1 TO TANK 2
THE WASTE LIQUOR IS PUMPED BY THE PUMP P2 INSIDE THE AOP REACTORS. WHEN THE REACTORS ARE COMPLETELY FILLED UP THE UV LAMPS ARE ACTIVATED FOR A PREDETERMINED TIME, THEN THE TREATED LIQUOR IS REPLACED END SENT IN THE TANK 2
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AOP Working Diagram
WORKING MODE 2CONTINOUS FROM TANK 1 TO TANK 2
THE WASTE LIQUOR IS PUMPED BY THE PUMP P2 INSIDE THE AOP REACTORS. WHEN THE REACTORS ARE COMPLETELY FILLED UP THE UV LAMPS ARE ACTIVATED. THEN THE PUMP IS AUTOMATICALLY ACTIVATED BY THE SYSTEM CONTROL WHICH MAINTAIN A LIQUOR FLOW FROM 4 TO 60 LITERS PER HOURS. THE TREATED LIQUOR IS SENT TO THE TANK 2
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AOP Working Diagram
WORKING MODE 3CONTINOUS RECICLING INSIDE AOP
THE WASTE LIQUOR IS PUMPED BY THE PUMP P2 INSIDE THE AOP REACTORS. WHEN THEREACTORS ARE COMPLETELY FILLED UP THE UV LAMPS ARE ACTIVATED. THE VALVE V6CLOSE, THE VALVE V12 OPENS AND THE VALVE V7 OPENS THE WAY FROM V12 TO THEPUMP P2THE PUMP P2 IS ACTIVATED AND THE LIQUOR IS CONTINOUSLY RECICLED INSIDE AOP FORTHE PRESET TIMEAT THE END OR THE TREATMENT TIME THE TREATED LIQUOR IS REPLACED AND SENT INTHE TANK 2
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AOP Working Diagram
WORKING MODE 4 CONTINOUS RECICLING FROM TANK 1 TO AOP
THE WASTE LIQUOR IS PUMPED BY THE PUMP P2 INSIDE THE AOP REACTORS. WHEN THE REACTORS ARE COMPLETELY FILLED UP THE UV LAMPS ARE ACTIVATED. THE VALVE V12 OPENS AND THE VALVE V7 OPENS THE WAY FROM V12 TO THE TANK 1THE PUMP P2 IS ACTIVATED AND THE LIQUOR IS CONTINOUSLY RECICLED FROM THE TANK 1 TO THE AOP FOR THE PRESET TIMEAT THE END OR THE TREATMENT TIME THE TREATED LIQUOR IS SENT TO THE TANK 2
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