NANOFILTRATON 
APPLICATION.
SEPERATION OF AMOXICILIN FROM 
PHARMACEUTICAL WASTEWATER. 
 Polyamide spiral wound nanofiltration (NF) membrane was evaluated for 
the treatment of amoxicillin wastewater. 
 Amoxicillin, 6-(R-hydroxy-a-amino phenyl acetamido) penicillanic acid is 
the only phenolic penicillin which is used as an antibacterial drug. 
 It is frequently used as antibiotic to treat many kinds of infections. 
 The presence of amoxicillin,potential to promote bacterial resistance as 
well as trigger long term adverse human health effects.
 NF membranes retain matters that can penetrate ultrafiltration 
(UF) membranes but some low molecular weight micropollutants 
that can be rejected by Reverse Osmosis (RO) membranes 
 The nominal molecular weight cut-off (MWCO) of NF membranes 
is in the range of 100-1000 Da. 
 MWCO is molecular weight of the molecule that is 90% retained 
by the membrane Therefore the molecular weight of antibiotics is 
coincident with the range of MWCO of NF membranes and the 
noticeable difference in molecular weight between amoxicillin and 
other materials in the amoxicillin wastewater makes it possible for 
them to be separated effectively with NF membranes.
DAIRY INDUSTRY 
 Nanofiltration membrane with specific pores size is 
possible to separate specific components of milk and whey. 
 In dairy industry, nanofiltration mainly used for special 
application such 
 partial demineralisation of whey, 
 lactose-free milk or , 
 volume reduction of whey
 Application of nanofiltration can performe separation such 
 Color removal 
 Demineralisation 
 Desalination 
 Type of dairy product that produced in application of 
nanofiltration 
 Milk 
 Cheese 
 Whey
 Milk has own concentration for some type of dairy, protein 
standardization and whey protein separation. 
 Whey is watery portion of milk that remaining after 
 milk coagulation 
 removal of curd
Dairy Industry for concentration 
and partial Demineralisation 
 In whey and permeates, nanofiltration will decrease 
mineral content especially for 
 Sodium 
 Potassium chloride 
 Both sodium and potassium chlorides are monovalent ion in 
dairy product. 
 Whey and permeates need pass through concentration 
step prior to further processing and combines volumes 
reduction with partial demineralisation.
 For saving transportation cost, nanofiltration for volume 
reduction (concentration) of whey and permeates must be 
applied. 
 It will increase flux rates 
 Lactose can be concentrated before next process. It will 
 Decrease amount of mineral and, 
 Increase efficient crystallisation process
 Lactose product has higher degree of purity 
 Permeate in nanofiltration contains, 
 Salt 
 Nitrogen 
 Lactose (some)
 Losses nitrogen and lactose in permeate, depends on 
 nanofiltration membrane characteristics 
 pre-treatment of feed 
 process condition
Dairy Industry for lactose 
reduction and detergent recovery. 
 Membrane layer in nanofiltration technology rejects 
lactose, but allows passage of various materials 
 Milk will maintain most original composition 
 Consumer will get sensory experience which almost similar 
to fresh milk
 Detergent recovery has purification of cleaning in place 
(CIP) solution 
 When detergent consumption higher, nanofiltration can 
achieve purification solution by using NaOH and HNO3 
 Loss of detergent removal of impurities and reduction of 
COD level 
 Enable very long recycling period to rduce in minimum
WASTEWATER TREATMENT 
 For waste water treatment, application of nanofiltration is 
applied in removal of cyanobacterial metabolites: 
 two treated water 
 production of drinking water 
 Cynobacteria metabolites are major problem that 
contributes for water industry: 
 produces toxic 
 taste and odour compound that make drinking water 
aesthetically displeasing
 process cynobacterial metabolites can be removed in very 
efficient due to larger compound than the pore size of 
nanofiltration membrane theorecticallly be removed by 
size exclusion. 
 Nanofiltration more often used due to the micro pollutants 
great rejection reached in contaminated water 
treatments. 
 an alternative to superficial water treatment for portable 
water production
RECOVERY of COPPER FROM ACID 
RINSE WATER. 
 An existing mining operation, using an acid leaching process 
for copper recovery, was confronted with two problems 
which prevented further expansion, namely. 
 (i) water in the mine’s area was scarce, and new wells 
expensive to drill 
 (ii) neutralization of spent sulphuric acid resulted in 
large sludge volumes with 2–3 mg/l residual copper.
 To overcome these limitations, acid rinse line was 
introduced to the feed tank at a pH of 1.2 and copper 
content of 1230 ppm. 
 This was pumped to a reverse osmosis system under high 
pressure (27–35 bar (g)) to concentrate the copper to 
8100 ppm, and it is possible to conentrate using RO, due to 
osmotic pressures exerted by the sulphuric acid. 
 Nanofiltration membrane was therefore used to 
concentrate the copper further, as the acid will pass 
through the membrane without adding significantly to the 
osmotic pressure.
Textile Industry 
 When the wastewater of a textile factory is gathered and treated in 
an activated sludge system, nanofiltration can provide an 
additional purification that allows to reuse the filtered water as 
process water. 
 As a pretreatment for the membrane filtration, a sand filter was 
used. The pretreatment removed suspended and settleable solids, 
which was necessary to avoid fouling of the nanofiltration 
membranes, which would shorten the membrane lifetime 
dramatically
Application of Nanofiltration
Application of Nanofiltration

Application of Nanofiltration

  • 1.
  • 2.
    SEPERATION OF AMOXICILINFROM PHARMACEUTICAL WASTEWATER.  Polyamide spiral wound nanofiltration (NF) membrane was evaluated for the treatment of amoxicillin wastewater.  Amoxicillin, 6-(R-hydroxy-a-amino phenyl acetamido) penicillanic acid is the only phenolic penicillin which is used as an antibacterial drug.  It is frequently used as antibiotic to treat many kinds of infections.  The presence of amoxicillin,potential to promote bacterial resistance as well as trigger long term adverse human health effects.
  • 3.
     NF membranesretain matters that can penetrate ultrafiltration (UF) membranes but some low molecular weight micropollutants that can be rejected by Reverse Osmosis (RO) membranes  The nominal molecular weight cut-off (MWCO) of NF membranes is in the range of 100-1000 Da.  MWCO is molecular weight of the molecule that is 90% retained by the membrane Therefore the molecular weight of antibiotics is coincident with the range of MWCO of NF membranes and the noticeable difference in molecular weight between amoxicillin and other materials in the amoxicillin wastewater makes it possible for them to be separated effectively with NF membranes.
  • 4.
    DAIRY INDUSTRY Nanofiltration membrane with specific pores size is possible to separate specific components of milk and whey.  In dairy industry, nanofiltration mainly used for special application such  partial demineralisation of whey,  lactose-free milk or ,  volume reduction of whey
  • 5.
     Application ofnanofiltration can performe separation such  Color removal  Demineralisation  Desalination  Type of dairy product that produced in application of nanofiltration  Milk  Cheese  Whey
  • 7.
     Milk hasown concentration for some type of dairy, protein standardization and whey protein separation.  Whey is watery portion of milk that remaining after  milk coagulation  removal of curd
  • 8.
    Dairy Industry forconcentration and partial Demineralisation  In whey and permeates, nanofiltration will decrease mineral content especially for  Sodium  Potassium chloride  Both sodium and potassium chlorides are monovalent ion in dairy product.  Whey and permeates need pass through concentration step prior to further processing and combines volumes reduction with partial demineralisation.
  • 9.
     For savingtransportation cost, nanofiltration for volume reduction (concentration) of whey and permeates must be applied.  It will increase flux rates  Lactose can be concentrated before next process. It will  Decrease amount of mineral and,  Increase efficient crystallisation process
  • 10.
     Lactose producthas higher degree of purity  Permeate in nanofiltration contains,  Salt  Nitrogen  Lactose (some)
  • 11.
     Losses nitrogenand lactose in permeate, depends on  nanofiltration membrane characteristics  pre-treatment of feed  process condition
  • 12.
    Dairy Industry forlactose reduction and detergent recovery.  Membrane layer in nanofiltration technology rejects lactose, but allows passage of various materials  Milk will maintain most original composition  Consumer will get sensory experience which almost similar to fresh milk
  • 13.
     Detergent recoveryhas purification of cleaning in place (CIP) solution  When detergent consumption higher, nanofiltration can achieve purification solution by using NaOH and HNO3  Loss of detergent removal of impurities and reduction of COD level  Enable very long recycling period to rduce in minimum
  • 14.
    WASTEWATER TREATMENT For waste water treatment, application of nanofiltration is applied in removal of cyanobacterial metabolites:  two treated water  production of drinking water  Cynobacteria metabolites are major problem that contributes for water industry:  produces toxic  taste and odour compound that make drinking water aesthetically displeasing
  • 15.
     process cynobacterialmetabolites can be removed in very efficient due to larger compound than the pore size of nanofiltration membrane theorecticallly be removed by size exclusion.  Nanofiltration more often used due to the micro pollutants great rejection reached in contaminated water treatments.  an alternative to superficial water treatment for portable water production
  • 16.
    RECOVERY of COPPERFROM ACID RINSE WATER.  An existing mining operation, using an acid leaching process for copper recovery, was confronted with two problems which prevented further expansion, namely.  (i) water in the mine’s area was scarce, and new wells expensive to drill  (ii) neutralization of spent sulphuric acid resulted in large sludge volumes with 2–3 mg/l residual copper.
  • 17.
     To overcomethese limitations, acid rinse line was introduced to the feed tank at a pH of 1.2 and copper content of 1230 ppm.  This was pumped to a reverse osmosis system under high pressure (27–35 bar (g)) to concentrate the copper to 8100 ppm, and it is possible to conentrate using RO, due to osmotic pressures exerted by the sulphuric acid.  Nanofiltration membrane was therefore used to concentrate the copper further, as the acid will pass through the membrane without adding significantly to the osmotic pressure.
  • 18.
    Textile Industry When the wastewater of a textile factory is gathered and treated in an activated sludge system, nanofiltration can provide an additional purification that allows to reuse the filtered water as process water.  As a pretreatment for the membrane filtration, a sand filter was used. The pretreatment removed suspended and settleable solids, which was necessary to avoid fouling of the nanofiltration membranes, which would shorten the membrane lifetime dramatically