Fabrication of Reverse Osmosis Spiral Wound Membranes using Local Materials

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Fabrication of Reverse Osmosis Spiral Wound Membranes using Local Materials Associate Prof. Heba Abdallah Chemical Engineering & Pilot plant Dept. Engineering Research Division Flat Sheet Membrane Centre National Research Centre

INTRODUCTION The factors responsible for the rise in water consumption High standards of living -High population growth rate -Increasing urbanization and industrialization -Regional conflicts resulting in mass flow of internal migrants -Lack of public awareness http://www.ecomena.org/tag/water-scarcity-in-arab-world/ -Failure to adopt basic water conservation principles -Insufficient energy for seawater desalination

INTRODUCTION Water Problems in Egypt Contamination of water Mixing with sewage or agricultural or industrial wastes. The stability of water resources and high population growth rates Decline in per capita share of water in Egypt to 600 cubic meters per year. Nile River (Main source) Different forms of Human consumption Industry Agriculture Problems with upstream countries

Most problem solutions can be carried out by: Waste Water treatment Desalination In The Research Field - Application in Lab Scale. Problems Solutions - Application of Research Projects on the ground By applying these projects on pilot units to reach the optimum ways to implement these projects.

NRC and Flat sheet membrane group Accordingly, The flat sheet membranes group has been configured in NRC at 2014. The header of this group is Prof. Dr. Ahmed Shaban Vice President of the NRC Centre for Technical Affairs. National Research Center was purchased Spiral wound fabrication machines to facilitate production of pilot samples of spiral wound membranes modules and facilitate the Pilot experiments in desalination and water treatment

Goals of Flat membranes group in National Research Centre -Benefiting from our previous experience and researches in Membrane Fabrication, Nanomaterials, water treatment and Desalination to Design low power cost desalination and water treatment units. -Production of different kinds of membranes (MF, UF, NF, FO and RO) in large scale and in the form of spiral wound membrane modules to be applied in different applications. -Production of antifouling Membranes using different kinds of nanomaterials. -Designing of Low power desalination systems, To serve the coastal and remote areas

Previous work of group in Membrane field Egyptian Patent 2003 ( for water treatment) (Manufacture of Polyamide-6 using casting technique) for protein removal Polymeric blend membranes (for Desalination) Egyptian Patent 2015 (Fabrication of RO blend PES/CA membranes) Desalinate brackish Water 6000 ppm Salt rejection 99%,Permeate flux 21 L/m 2.h Low RO pressure membrane (15-20 bar)

Previous work of group in Membrane field For Water treatment Egyptian Patent 2015 Design and development of Polyamide-6 (PA-6) membranes for pervaporation of water /alcohols mixtures.

Previous work of group in Membrane field Nano materials blend membranes Polymer blend with Inorganic Nanotubes to produce high flux RO membranes, with low pressure Used to desalinate a wide range of salty concentrated solutions in range of ( 3000 ppm to 45000 ppm) SR (99-95%) with low pressure (15-30 bar) TEM analysis for TiO 2 dioxide nanotubes

Previous work of group in Membrane field Nano materials blend membranes Polymer blend with Metalorganic Nanomaterials To produce RO PES membranes Used to desalinate sea water 35000 ppm to 45000 ppm. The average flux 24.2 L/m 2 h with salt rejection 99.5%, with low pressure (20-30 bar) Decrease in RS (2.4µm PES to 0.24µm) SEM of metalorganic nanomaterials

Bottom Surface Previous work of group in Membrane field Forward osmosis membrane For low energy desalination system Top Surface Cross section

Recently, 2017 Fabrication of Spiral wound membranes

Fabrication of Spiral wound membranes Materials and Methods Different polymeric materials were used in membrane preparation, we selected new RO type which was blended PES with amine nano- solution to produce RO flat sheet without outside coating. We submitted a patent in this polymer membrane preparation for Egyptian Academy of Science & Technology in title: Fabrication of Antifouling Spiral Wound Reverse Osmosis Membranes supported by fabric (Patent No.1301/2016). We also, fabricated pilot scale casting machine using raw materials purchased from Egyptian local market and we progress to other patent in title: Design and manufacture of a device for the preparation of flat membranes (Patent No. 0167/2015). We also, designed and fabricated testing desalination unit using high pressure up to 200 bar. And we progress to other patent in title: Design, manufacture and test the unit cells of polymeric membranes (Patent No. 1852/2015)

Fabrication of Asymmetric RO Blend Membranes Polymeric solution preparation was casted using pilot casting machine Pilot casting machine RO produced membrane in size of 65x110 cm

Fabrication of Asymmetric RO Blend Membranes Units for membrane surface treatment and storing

Flat sheet membrane testing Flat sheet membranes exposed To gradually different high pressures from 15 to 100 bar. High pressure pump Up to 200 bar

Salt Rejection % Desalination Results of RO membranes 20000 35000 45000 Sea water (35800 ppm) 98 96 94 92 90 88 86 84 M1 M2 M3 Membranes Type M1: PES /AMS without support M2: PES /AMS with nonwoven support M3: PES /AMS with woven support Under 50 bar pressure

Mechanical Properties Desalination Results of RO membranes 160 140 120 100 80 60 40 20 0 152 Tensile strength, Kg/ sq m Elongation, mm M1 M2 M3 37 M1: PES /AMS without support M2: PES /AMS with nonwoven support M3: PES /AMS with woven support

Flat Sheet Membrane Housing *Low surface area and need large space *low Permeate flux *low rejection % *High surface area according to number of membranes *Small in Size and don t need large space *High Permeate flux *High rejection % Spiral wound membrane and Housing Flat Housing of Flat sheet membrane

What is spiral wound membrane It is layers of flat-sheet membranes and feed separators wrapped around a hollow core. Feed solutions enter one end of the element, flowing under pressure through the membrane into permeate channels, spiral to the central core, and exit as permeate. This configuration offers the highest membrane-packing area with the smallest footprint.

Fabrication of Spiral Wound Membrane Fiber glass coating Spiral wound module materials Seal Antitelscopiing device

Fabrication of Spiral Wound Membrane Rolling Trimming ( side cutting) Fiber glass winding

Product types

Fabrication of Spiral Wound Membrane

Low Power Desalination Pilot Units UF/RO integrated Pilot system RO spiral wound modules (4021) (two modules) Spiral wound membrane with local materials SR 99% Permeate flux 390.3 L/m 2.h

The Cost of Membranes The total cost of flat sheet membrane cost using fabricated casting machine is the 1125.4 L.E. /m 2. The price of commercial flat sheet membrane is around 300 $/m 2 [*]. Approx. 6000 L.E/m 2 flat sheet. RO Membrane module 4 x40 for sea water desalination 8 x 40 for Sea water desalination Imported modules [**] ($) without taxes and customs Imported modules (L.E) without taxes and customs Approx. price of produced spiral wound modules in NRC labs; Egypt 1090 $ 21,800 L.E 7,500 to 10,500 L.E 1778 $ 35,560 L.E 15,750 to 20,750 L.E [*] http://www.sterlitech.com/reverse-osmosis-ro-membrane.html [**] http://espwaterproducts.com/commercial-ro-membranes.htm.