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-
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