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Design and development of composite nonwoven filter forDesign and development of composite nonwoven filter for
pre-filtration of textile effluents using nano technologypre-filtration of textile effluents using nano technologyUnder the guidance of
Dr.J.P.Singh & Dr. Devendra prasad
UPTTI Kanpur
&
Dr. Anurag Shrivastava
DMSRDE Kanpur
By
Vivek Kumar Sharma
M.Tech- Textile technology
Department of Textile Technology
Uttar Pradesh Textile Technology Institute
Kanpur
AbstractAbstract
• Textile industries represent an important environment
problem due to their water consumption and produced
large amount of waste water. In many regions of world
with water scarcity, this fact can be an argument to make
wastewater cleaning necessary.
• This project discusses a Cleaner approach for minimization of
waste particle in dyeing effluent.
• The removal of stuff by Composite filter { Nanofibre
(polyethersulfone) film spread over nonwoven needle punched
fabric (Polyester)} was evaluated for reactive dye. Results showed
that membrane treatment is a promising advanced treatment option
for pollution control for textile industry effluents
IntroductionIntroduction
 For removing these types of metals and other particle textile industry use ETP
(effluent treatment plant). In this type of plant the removal of particle from the
water is done sufficiently. This type of plant runs with four stage of removing the
effluent. These are Preliminary, Primary, Secondary & tertiary treatment.
 Pressure-driven membrane filtration processes such as microfiltration (MF), ultra
filtration (UF), nano filtration (NF), and reverse osmosis (RO) provide opportunities
for the textile industry to better water by separating its components based on size.
However, widespread adoption of some of these processes has yet to be realized due
to membrane fouling. Membrane fouling is the accumulation of soil, or foulant, on
the surface or within the pores of a membrane. Fouling prolongs processing times,
increases energy and cleaning costs, decreases separation efficiency, and, in severe
cases, may lead to irreversible clogging of the membrane.
 So our aim to develop a composite filter for prefiltration of textile effluents. if the pre
filtration of textile effluent is good the other next process results will go even better.
Development of Composite MembraneDevelopment of Composite Membrane
• We all know that non woven fabric is mostly used for filtration process of water for
her messing structure.
• Applying the Nanofibre over it is give control the pore size and give even better
filtration results.
•PES was selected as the Nanofibre membrane material due to its high thermal and
chemical resistance also its appropriate mechanical properties.
Material & MethodMaterial & Method
1. Preparation of nonwoven material
2. Spreading of Nanofibre over Nonwoven
material
3. Preparation of wastewater
4. Filtration
Preparation of nonwoven materialPreparation of nonwoven material
 In this project we manufacture nonwoven by regenerated
round shaped polyester fibre (staple length 51mm and
fineness 1.5 denier) by UPTTI lab model machine (model-
Trytex) with two different weight sample of 130 and 198 gsm.
Sr.
No.
Parameters Sample A
(20 gram fibre)
Each 3 Sample
Sample B
(30 gram fibre)
Each 3 Sample
1 Sample Size 10x25 inch 10x25 inch
2 Weight of sample 20 gm 30 gm
3 GSM of sample 130 195
4 Pore size 50-300 50-300
5 Thickness 2.1 mm (approx) 3.5 mm (approx)
Machine parameter
1 Feed mm /Stroke 10 10
2 Punches /min 35 35
Preparation of NanofibrePreparation of Nanofibre
• Polyethersulfone (PES) (Mw= 58000 and density of 1.37 g/cm3) was
from DMSRDE lab. As the sub layer of the membrane a technical
polyester non-woven was used. The chemical structure of PES and
DMF is shown in figure. The solvents N,Ndimethylformamide (DMF)
were obtained from DMSRDE lab.
Polyethersulfone (PES) N,Ndimethylformamide
Solution viscosity -
. PES (%) Viscosity (Pa s)
15 0.52
Electro spinning conditionsElectro spinning conditions
Sr. No. Parameter PES nanofibrous
Membrane
(first)
PES nanofibrous
Membrane
(Second)
PES nanofibrous
Membrane
(third)
1 PES Concentration 15wt% 15wt% 15wt%
2 Applied voltage 20 kV 20 kV 20 kV
3 Feed rate 25 micro lt/min 25 micro lt/min 25 micro lt/min
4 Spinning distance 25 cm 25 cm 25 cm
5 Collection time 2 h 3 h 5 h
6
outer diameter of the
injector
15 mm 15 mm 15 mm
No of sampleNo of sample
 Preparing a waste water Sample with Medium shade Using Salt
Concentration 20g/l Nacl, 8g/l Na2CO3 & Dye 50 mg/Lit
• We prepared sample of both GSM nonwoven fabric with three different
time spreading. (total sample =6)
Sr. No. Sample no. Classification
1 S1 130 GSM + 2 Hour Spreading
2 S2 130 GSM + 3 Hour Spreading
3 S3 130 GSM + 5 Hour Spreading
4 S4 198 GSM + 2 Hour Spreading
5 S5 198 GSM + 3 Hour Spreading
6 S6 198 GSM + 5
Hour Spreading
UV RESULTSUV RESULTS
Company DMSRDE
[Detailed Information]
Creation date 11/3/2016 4:42 AM
Data array type Linear data array
Horizontal axis Wavelength [nm]
Vertical axis Abs
Start 800 nm
End 200 nm
Data interval 1 nm
Data points 601
[Measurement Information]
Instrument name spectrophotometer
Model name V-630
Serial No. B187161148
Accessory USE-753
Accessory S/NB187161148
Cell length 10 mm
Photometric mode Abs
Measurement range 800 - 200 nm
Data interval 1 nm
UV/Vis bandwidth 1.5 nm
Response Medium
Scan speed 200 nm/min
Change source at 340 nm
Light source D2/WI
Filter exchange Step
Correction Baseline
Parameters-
UV RESULTSUV RESULTS
Absorption Value
UV
VALUE
Before
filtration
After
Filtration
Main Sample
130 GSM+ 2
Hours
130 GSM +
3Hours
103 GSM +
5Hours
198 GSM + 2
Hours
198 GSM + 3
Hours
198 GSM + 5
Hours
800 1.71591 0.520248 0.490538 0.460582 0.343146 0.281131 0.109926
799 1.71545 0.519843 0.49034 0.45977 0.343158 0.281105 0.110076
700 1.63816 0.482494 0.462668 0.393183 0.320951 0.273147 0.106418
600 1.5975 0.462997 0.446871 0.367181 0.307864 0.26762 0.108035
500 1.72512 0.601857 0.61504 0.501424 0.446751 0.423599 0.300661
462 4.48165 2.59514 2.95018 2.43993 2.39472 2.36918 2.60564
461 7 2.69383 3.03568 2.53488 2.49018 2.46368 2.68427
130 GSM & 198 GSM sample absorption in130 GSM & 198 GSM sample absorption in
different UV value (comparison)different UV value (comparison)
200 300 400 500 600 700 800
0
1
2
3
4
5
6
7
8Abs
UV Value
Main Sample
130 gsm+ 2 hours
130 gsm + 3hours
130 gsm + 5 hours
198 gsm +2 Hours
198gsm+3 hours
198 gsm +5 hours
Comparison flux rate of different type of sample throughComparison flux rate of different type of sample through
dyeing waste water and fresh waterdyeing waste water and fresh water
ConclusionConclusion
1. Results Show that the ion and other particle concentration will decrease in
all filtered sample from main sample.
2. Result Show that the flux permeability value and permeate flux will
decrease simultaneously according to thickness of nonwoven fabric and
also Nanofibre.
3. The removal efficiency of composite sample is 75%. & we know the
Microfiltration cleaning efficiency is 70 %.
4. So if we use this filter for pre-filtration of microfiltration process. We
achieve the cleaning efficiency around 91% of textile effluent.
AcknowledgementAcknowledgement
• It gives me immense pleasure to express my deep sense of gratitude & whole hearted thanks
to my college authority & DMSRDE authority for giving me opportunity to work on this
project.
• I am thankful to Dr. D.B.Shakyawar (Director, U.P.T.T.I) & Dr. Anurag Shrivastava
Sc-“G” ( Add. Director & Head-Department of Technical Textile, DMSRDE) in this regard.
• I am immense grateful to Dr. J.P.Singh (Project Guide) Dr. K. Mukophadhyaya Sc-“F”-
(Head- Department of Nano materials DMSRDE) & Dr. Debmalya Roy Sc-“E”-
(Department of Nano materials DMSRDE) for his valuable guidance, generous advice, critical
observations & benevolent approach which all our work & exercise to achieve something
worthwhile & satisfactory from a technical point of view.
• I am also like to thank to all DMSRDE Lab Staff & weaving lab staff- UPTTI for their
immense support in the lab.
• Last but not the least we also acknowledge the direct indirect effort & support of all the
members of UPTTI & DMSRDE for their continuous co-operation during project duration &
making this learning experience a truly successful one

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Presentation

  • 1. Design and development of composite nonwoven filter forDesign and development of composite nonwoven filter for pre-filtration of textile effluents using nano technologypre-filtration of textile effluents using nano technologyUnder the guidance of Dr.J.P.Singh & Dr. Devendra prasad UPTTI Kanpur & Dr. Anurag Shrivastava DMSRDE Kanpur By Vivek Kumar Sharma M.Tech- Textile technology Department of Textile Technology Uttar Pradesh Textile Technology Institute Kanpur
  • 2. AbstractAbstract • Textile industries represent an important environment problem due to their water consumption and produced large amount of waste water. In many regions of world with water scarcity, this fact can be an argument to make wastewater cleaning necessary. • This project discusses a Cleaner approach for minimization of waste particle in dyeing effluent. • The removal of stuff by Composite filter { Nanofibre (polyethersulfone) film spread over nonwoven needle punched fabric (Polyester)} was evaluated for reactive dye. Results showed that membrane treatment is a promising advanced treatment option for pollution control for textile industry effluents
  • 3. IntroductionIntroduction  For removing these types of metals and other particle textile industry use ETP (effluent treatment plant). In this type of plant the removal of particle from the water is done sufficiently. This type of plant runs with four stage of removing the effluent. These are Preliminary, Primary, Secondary & tertiary treatment.  Pressure-driven membrane filtration processes such as microfiltration (MF), ultra filtration (UF), nano filtration (NF), and reverse osmosis (RO) provide opportunities for the textile industry to better water by separating its components based on size. However, widespread adoption of some of these processes has yet to be realized due to membrane fouling. Membrane fouling is the accumulation of soil, or foulant, on the surface or within the pores of a membrane. Fouling prolongs processing times, increases energy and cleaning costs, decreases separation efficiency, and, in severe cases, may lead to irreversible clogging of the membrane.  So our aim to develop a composite filter for prefiltration of textile effluents. if the pre filtration of textile effluent is good the other next process results will go even better.
  • 4. Development of Composite MembraneDevelopment of Composite Membrane • We all know that non woven fabric is mostly used for filtration process of water for her messing structure. • Applying the Nanofibre over it is give control the pore size and give even better filtration results. •PES was selected as the Nanofibre membrane material due to its high thermal and chemical resistance also its appropriate mechanical properties.
  • 5. Material & MethodMaterial & Method 1. Preparation of nonwoven material 2. Spreading of Nanofibre over Nonwoven material 3. Preparation of wastewater 4. Filtration
  • 6. Preparation of nonwoven materialPreparation of nonwoven material  In this project we manufacture nonwoven by regenerated round shaped polyester fibre (staple length 51mm and fineness 1.5 denier) by UPTTI lab model machine (model- Trytex) with two different weight sample of 130 and 198 gsm. Sr. No. Parameters Sample A (20 gram fibre) Each 3 Sample Sample B (30 gram fibre) Each 3 Sample 1 Sample Size 10x25 inch 10x25 inch 2 Weight of sample 20 gm 30 gm 3 GSM of sample 130 195 4 Pore size 50-300 50-300 5 Thickness 2.1 mm (approx) 3.5 mm (approx) Machine parameter 1 Feed mm /Stroke 10 10 2 Punches /min 35 35
  • 7. Preparation of NanofibrePreparation of Nanofibre • Polyethersulfone (PES) (Mw= 58000 and density of 1.37 g/cm3) was from DMSRDE lab. As the sub layer of the membrane a technical polyester non-woven was used. The chemical structure of PES and DMF is shown in figure. The solvents N,Ndimethylformamide (DMF) were obtained from DMSRDE lab. Polyethersulfone (PES) N,Ndimethylformamide Solution viscosity - . PES (%) Viscosity (Pa s) 15 0.52
  • 8. Electro spinning conditionsElectro spinning conditions Sr. No. Parameter PES nanofibrous Membrane (first) PES nanofibrous Membrane (Second) PES nanofibrous Membrane (third) 1 PES Concentration 15wt% 15wt% 15wt% 2 Applied voltage 20 kV 20 kV 20 kV 3 Feed rate 25 micro lt/min 25 micro lt/min 25 micro lt/min 4 Spinning distance 25 cm 25 cm 25 cm 5 Collection time 2 h 3 h 5 h 6 outer diameter of the injector 15 mm 15 mm 15 mm
  • 9. No of sampleNo of sample  Preparing a waste water Sample with Medium shade Using Salt Concentration 20g/l Nacl, 8g/l Na2CO3 & Dye 50 mg/Lit • We prepared sample of both GSM nonwoven fabric with three different time spreading. (total sample =6) Sr. No. Sample no. Classification 1 S1 130 GSM + 2 Hour Spreading 2 S2 130 GSM + 3 Hour Spreading 3 S3 130 GSM + 5 Hour Spreading 4 S4 198 GSM + 2 Hour Spreading 5 S5 198 GSM + 3 Hour Spreading 6 S6 198 GSM + 5 Hour Spreading
  • 10. UV RESULTSUV RESULTS Company DMSRDE [Detailed Information] Creation date 11/3/2016 4:42 AM Data array type Linear data array Horizontal axis Wavelength [nm] Vertical axis Abs Start 800 nm End 200 nm Data interval 1 nm Data points 601 [Measurement Information] Instrument name spectrophotometer Model name V-630 Serial No. B187161148 Accessory USE-753 Accessory S/NB187161148 Cell length 10 mm Photometric mode Abs Measurement range 800 - 200 nm Data interval 1 nm UV/Vis bandwidth 1.5 nm Response Medium Scan speed 200 nm/min Change source at 340 nm Light source D2/WI Filter exchange Step Correction Baseline Parameters-
  • 11. UV RESULTSUV RESULTS Absorption Value UV VALUE Before filtration After Filtration Main Sample 130 GSM+ 2 Hours 130 GSM + 3Hours 103 GSM + 5Hours 198 GSM + 2 Hours 198 GSM + 3 Hours 198 GSM + 5 Hours 800 1.71591 0.520248 0.490538 0.460582 0.343146 0.281131 0.109926 799 1.71545 0.519843 0.49034 0.45977 0.343158 0.281105 0.110076 700 1.63816 0.482494 0.462668 0.393183 0.320951 0.273147 0.106418 600 1.5975 0.462997 0.446871 0.367181 0.307864 0.26762 0.108035 500 1.72512 0.601857 0.61504 0.501424 0.446751 0.423599 0.300661 462 4.48165 2.59514 2.95018 2.43993 2.39472 2.36918 2.60564 461 7 2.69383 3.03568 2.53488 2.49018 2.46368 2.68427
  • 12. 130 GSM & 198 GSM sample absorption in130 GSM & 198 GSM sample absorption in different UV value (comparison)different UV value (comparison) 200 300 400 500 600 700 800 0 1 2 3 4 5 6 7 8Abs UV Value Main Sample 130 gsm+ 2 hours 130 gsm + 3hours 130 gsm + 5 hours 198 gsm +2 Hours 198gsm+3 hours 198 gsm +5 hours
  • 13. Comparison flux rate of different type of sample throughComparison flux rate of different type of sample through dyeing waste water and fresh waterdyeing waste water and fresh water
  • 14. ConclusionConclusion 1. Results Show that the ion and other particle concentration will decrease in all filtered sample from main sample. 2. Result Show that the flux permeability value and permeate flux will decrease simultaneously according to thickness of nonwoven fabric and also Nanofibre. 3. The removal efficiency of composite sample is 75%. & we know the Microfiltration cleaning efficiency is 70 %. 4. So if we use this filter for pre-filtration of microfiltration process. We achieve the cleaning efficiency around 91% of textile effluent.
  • 15. AcknowledgementAcknowledgement • It gives me immense pleasure to express my deep sense of gratitude & whole hearted thanks to my college authority & DMSRDE authority for giving me opportunity to work on this project. • I am thankful to Dr. D.B.Shakyawar (Director, U.P.T.T.I) & Dr. Anurag Shrivastava Sc-“G” ( Add. Director & Head-Department of Technical Textile, DMSRDE) in this regard. • I am immense grateful to Dr. J.P.Singh (Project Guide) Dr. K. Mukophadhyaya Sc-“F”- (Head- Department of Nano materials DMSRDE) & Dr. Debmalya Roy Sc-“E”- (Department of Nano materials DMSRDE) for his valuable guidance, generous advice, critical observations & benevolent approach which all our work & exercise to achieve something worthwhile & satisfactory from a technical point of view. • I am also like to thank to all DMSRDE Lab Staff & weaving lab staff- UPTTI for their immense support in the lab. • Last but not the least we also acknowledge the direct indirect effort & support of all the members of UPTTI & DMSRDE for their continuous co-operation during project duration & making this learning experience a truly successful one