Content uploaded by Sunanda Kore
Author content
All content in this area was uploaded by Sunanda Kore
Content may be subject to copyright.
Universal Journal of Environmental Research and Technology
All Rights Reserved Euresian Publications © 2011 eISSN 2249 0256
Available Online at: www.environmentaljournal.org
Volume 1, Issue 3: 233-238
Open Access Review Article
233
Garud et al.
A Short Review on Process and Applications of Reverse Osmosis
*Garud R. M., Kore S. V., Kore V. S., Kulkarni G. S.
1
Department of Environmental science and Technology, Shivaji University, Kolhapur (Maharashtra)
*Corresponding author: ravindragarud65@gmail.com
Abstract:
Reverse Osmosis (RO) is a membrane based process technology to purify water by separating the dissolved
solids from feed stream resulting in permeate and reject stream for a wide range of applications in domestic as
well as industrial applications. It is seen from literature review that RO technology is used to remove dissolved
solids, colour, organic contaminants, and nitrate from feed stream. Hence RO technology used in the treatment
of water and hazardous waste, separation processes in the food, beverage and paper industry, as well as
recovery of organic and inorganic materials from chemical processes as an alternative method . This paper
intends to provide an overall vision of RO technology as an alternative method for treating wastewater in
different Industrial applications. The present short review shows applicability of RO system for treating effluents
from beverage industry, distillery spent wash, ground water treatment, recovery of phenol compounds, and
reclamation of wastewater and sea water reverse osmosis (SWRO) treatment indicating efficiency and
applicability of RO technology.
Keywords:
Beverage Industry, Boiler Feed Water, Distillery Spent Wash, Recovery of Phenol Compounds,
Reclamation of Wastewater, Sea Water Reverse Osmosis
1.0 Introduction:
Reverse Osmosis (RO) is a process that uses semi-
permeable spiral wound membranes to separate and
remove dissolved solids, organic, pyrogens,
submicron colloidal matter, color, nitrate and
bacteria from water. Feed water is delivered under
pressure through the semi permeable membrane,
where water permeates the minute pores of the
membrane and is delivered as purified water called
permeate water. Impurities in the water are
concentrated in the reject stream and flushed to the
drain is called reject water. These membranes are
semi-permeable and reject the salt ions while letting
the water molecules pass. The materials used for RO
membranes are made of cellulose acetate,
polyamides and other polymers. The membrane
consists of hollow-fiber, spiral-wound used for
treatment; depend on the feed water composition
and the operation parameters of the plant. Reverse
Osmosis (RO) is a membrane based process
technology used for desalination. Membrane-based
seawater desalination and wastewater reuse are
widely considered as promising solutions to augment
water supply and alleviate water scarcity (S. Lee et
al., 2010). The most common membrane processes
used are the reverse osmosis (RO) and the electro
dialysis (ED) used for brackish water desalination,
but only RO competes with distillation processes in
seawater desalination (Kalogirou, 2005).
1.1 Scope of Reverse Osmosis:
The process has also been applied to treat municipal
wastewater. Since conventional municipal treatment
processes do not remove dissolved solids, but RO
process is used for the removal of dissolved solids.
RO is increasingly used as a separation technique in
chemical and environmental engineering for the
removal of organics and organic pollutants present
in wastewater. It is seen from literature review that
Reverse Osmosis (RO) processes have been widely
used for separation and concentration (recovery) of
solutes in many fields.
The use of RO in the treatment of various effluents
of chemical (Bodalo-Santoyo et al.,2004; Bodalo-
Santoyo et al., 2003), petrochemical,
electrochemical, food, paper and tanning industries
as well as in the treatment of municipal waste
waters have been reported in the literature and
were studied by many researcher (Schutte et al.,
2003). Removal of organic contaminants by RO
Universal Journal of Environmental Research and Technology
234
Garud et al.
processes was first demonstrated by Chian et al.
(1975). The presence of individual contaminants
can cause problems, hence the removal of individual
contaminants by RO has been studied by very few
researchers (Murthy et al., 1999; Moresi et al., 2002;
Arsuaga et al., 2006). Murthy and Choudhari (2008)
studied the paper on “Treatment of Distillery Spent
Wash where UF and RO membranes used for
purification of the wastewater by removing the
colour and the contaminants. A number of
studies(Kimura et al.,2003; Bellona et al., 2004; Xu et
al.,2005) have been reported on the application of
RO for the removal of Organics such as endocrine
disrupting chemicals, plastic additives, pesticides,
pharmaceutically active compounds (PhaC’s),
benzene and toluene. Cellulose acetate and
polyamide membrane has good salt rejection for
inorganic salts like NaCl, Na
2
SO
4
-
.
However, for
organics, the rejection is reported to be lower and
varies widely in the range of 0.3-0.96 (Pozderivic et
al., 2006; Senthilmurugan and Gupta, (2006). RO
process removes fluoride proportionately, if TDS is at
tolerable level and fluoride content is high then one
can use special alum-resin filter, works under
gravitational force. (Krishnan S. et al., 2005).
1.2 Treatment options for Reverse
Osmosis:
In India, distillery uses various forms of primary,
secondary and tertiary treatments of wastewater.
The units processes used are screening and
equalization, followed by biomethanation. Ferti-
irrigation and biocomposting with sugarcane
pressmud are the most widely used options for
effluent disposal (Ramana et al., 2002).In case of
grain based distillery the treatment given is by way
of DWGS separation, incineration and
biomethanation. The process streams that can be
recycled are namely, thin slop and process
condensate. The effluent generated after removal of
the solids. Thin slop contain high TDS, high
temperature and contain carbohydrates, organic
acids, dead yeast cells etc. which may have an
impact on the fermentation process. The process
condensate from the evaporator has high
temperature, low pH, organic acids etc. This can be
treated by RO system and used in the process or for
utility operations.
1.3 Reverse Osmosis Process Description:
The RO process is simple in design consisting of feed,
permeate and reject stream. For feed water it is
necessary to provide pretreatment in order to
remove inorganic solids and suspended solid and
using high pressure pump given feed through semi
permeable membrane. Depending upon the
permeate where it is used necessary post treatment
is given. A schematic diagram of the RO process is
shown figure 1.
Figure1. Schematic Diagram of the RO Process
1.4 Reverse Osmosis Requisites:
An RO desalination plant essentially consists of four
major systems: (a) Pretreatment system, (b) High-
pressure pumps, (c) Membrane systems, and (d)
Post-treatment. Pre-treatment system is provided to
remove all suspended solids so that salt precipitation
or microbial growth does not occur on the
membranes. Pre-treatment may involve
conventional methods like a chemical feed followed
by coagulation/ flocculation/sedimentation, and
sand filtration or membrane processes i.e micro
filtration (MF) and ultra filtration (UF). High-pressure
pumps supply the pressure needed to enable the
Universal Journal of Environmental Research and Technology
235
Garud et al.
water to pass through the membrane and have the
salt rejected. The pressure ranges from 17 to 27 bar
for brackish water, and from 52 to 69 bar for
seawater. Membrane systems consist of a pressure
vessel and a semi-permeable membrane inside that
permits the feed water to pass through it. RO
membranes for desalination generally come in two
types: Spiral wound and Hollow fiber. Depending
upon water quality of permeate and use of
permeate; post treatment may consists of adjusting
the pH and disinfection (Djebedjian et al, 2006).
1.5 Membrane Characteristics:
The membrane should be inexpensive, have longer
and stable life. Membrane should be easily
manufactured with good salt rejection i.e. slightly
permeable to salt. They should have high water flux
i.e highly permeable to water and less susceptible to
fouling. They should permit the flow of large
amounts of water through the membrane relative to
the volume they occupy. The membrane should
chemically, physically and thermally stable in saline
waters. They need to be strong enough to withstand
high pressures and variable feed water quality.
1.6 Advantages of RO Process:
Following are the advantages of the RO process that
make it attractive for dilute aqueous wastewater
treatment include:
(1) RO systems are simple to design and operate,
have low maintenance requirements, and are
modular in nature, making expansion of the systems
easy;
(2) Both inorganic and organic pollutants can be
removed simultaneously by RO membrane
processes;
(3) RO systems allow recovery/recycle of waste
process streams with no effect on the material being
recovered;
(4) RO systems require less energy as compared to
other technology; and
(5) RO processes can considerably reduce the
volume of waste streams so that these can be
treated more efficiently and cost effectively by other
processes such as incineration (Cartwright, 1985;
Sinisgalli and McNutt, 1986; Cartwright, 1990;
McCray et al., 1990; Cartwright, 1991; Williams et
al., 1992).
(6) The RO plant is normally operated at ambient
temperature which reduces the scale formation and
corrosion problems, because of antiscalent and
biodispersent use, which will reduce maintenance
cost.
(7) The modular structure of the RO process
increases flexibility in building desalination plants
within a wide range of capacities.
(8) The specific energy requirement is significantly
low 3- 9.4 kW h/m
3
product.
(9) The process is electrically driven hence it is
readily adaptable to powering by solar panels.
In addition, RO systems can replace or be used in
conjunction with others treatment processes such as
oxidation, adsorption, stripping, or biological
treatment (as well as many others) to produce high
quality product water that can be reused or
discharged.
2.0 Applications of Reverse Osmosis:
This technology has advantage of a membrane based
process where concentration and separation is
achieved without a change of state and without use
of chemicals or thermal energy, thus making the
process energy efficient and ideally suited for
recovery applications. The bibliographic review
shows applicability of RO system for treating
effluents from beverage industry, distillery spent
wash, ground water treatment, recovery of phenol
compounds, and reclamation of wastewater and sea
water reverse osmosis (SWRO) treatment indicating
efficiency and applicability of RO technology.
2.1 Distillery Spent Wash:
The spent wash in distillery is acidic having pH 3.94
-4.30, dark brown liquid with high BOD 45000–
100000 mg/ l and COD 90000 – 210000 mg/ l, and
emits obnoxious odour but do not contain toxic
substances, when discharged in water streams
gives immediate discoloration and depletion of
dissolved oxygen , posing serious threat to the
aquatic flora and fauna (Mane et al., 2006).
Membrane based separation processes like ultra
filtration (UF), nano filtration (NF), reverse osmosis
(RO) and membrane bioreactor (MBR) have been
applied for treating distillery effluent (Nataraj et al.,
2006; Couallier et al., 2006; Zhang et al., Murthy
And Chaudhari;2006). Murthy and Choudhari (2008)
studied the paper on “Treatment of Distillery Spent
Wash where UF and RO membranes on pilot plant
uses thin film composite membrane for purification
of the wastewater for removal of colour and the
contaminants. The result obtained which indicate
suitability of RO for reducing freshwater
consumption by recycling water which will minimize
the waste disposal costs and reduction in regulatory
pressure. The pilot plant gives removal of Total
Universal Journal of Environmental Research and Technology
236
Garud et al.
Dissolved Solids (TDS), Chemical Oxygen Demand
(COD), Biochemical Oxygen Demand (BOD), sulphate
and potassium with the rejection efficiency of 97.9%,
96.8%, 97.9%, 99.7% and 94.65%, respectively. The
above results were obtained for feed flow of 15
lit/min and feed pressure of 20 atm. They found TDS
in permeate water less than 1000 ppm and COD 500
ppm i.e. within limits as per the guidelines of the
World Health Organization(WHO) and the Central
Pollution Control Board (CPCB) of India.
2.2 Ground Water Treatment:
Belkacem et al. (2006), studied ground water
treatment in which two stage RO module was used
in the beverage industry. The results of the physico-
chemical analysis showed that the raw water taken
from the groundwater contained significant amounts
of solutes and suspended solids (TDS ranging from
757 mg/l to 964 mg/l). The Feed water composition
shows that the raw water was rich in sulphate,
chloride and calcium and highly furring. The quality
of water produced from the pre-treatment
demonstrates that turbidity underwent the
strongest reduction 87% i.e. reduced from 1.3 NTU
to 0.167 NTU. The rejection rate varied between
97% and 98% and remained stable during the RO
operation which signified that the permeate quality
was constant with total conductivity decreased from
1070 µs/cm to 33 µs/cm with larger rejection of 95
% ions. The bacteria removal efficiency of
microorganisms decreased from 90 UFC/100 ml to
50 UFC/100 ml, which represents a total elimination
of 44%. However, the rejection of nitrate was lowest
i.e about 88.18%. Hence the obtained results
showed applicability of RO for the ground water
treatment.
2.3 Recovery of Phenol Compounds:
Kurihara et al. (1981) uses Toray composite
membrane PEC-1000 (polyfuran) and found several
organic rejections with 97% for acetone and 99% for
phenol. Koyama et al. (1982) and Koyama et al.
(1984) reported separation results for several polar
organic solutes (alcohols, phenols, carboxylic acids,
amines, and ketones) and various phenolic
derivatives for a composite membrane. They found
that the main factors affecting rejection included
molecular weight, molecular branching, polarity, and
degree of dissociation for ionizable compounds.
Bhattacharyya et al. (1987) and Bhattacharyya and
Madadi (1988) investigated rejection and flux
characteristics of FT30 membranes for separating
various pollutants (PAHs, chloro phenols, nitro
phenols) and found membrane rejections were
more than (>98%) for the organics under ionized
conditions. They also found substantial water flux
decline occurred even for dilute (< 50 mg/L)
solutions of non ionized organics and observed
significant organic adsorption on the membrane in
some cases. Pusch et al. (1989) reported separation
results for several different membranes (four
composite and two asymmetric) for a variety of
single and multi component organic solutions,
including many organic pollutants. Rejections varied
from only 25% up to >99% depending on the solute,
but generally the composite membrane rejections
were higher.
Srinivasan et al. (2010), conducted experiments for
the recovery of phenol compounds on a laboratory
scale on spiral wound polyamide RO module and
parameter were studied. The Perma-TFC polyamide
RO membrane in Spiral wound configuration
(supplied by Permionics, Vadodara, India) were used
in their study. It was found that the value of
rejection increases with the increasing applied
pressure. The maximum rejection obtained is around
90% for phenol.
2.4 Reclamation of wastewater:
The wastewaters contain organic contaminants,
including pharmaceutical compounds, pathogens,
disinfection by-products, and pesticides. They are
less affected by biological degradation by bacteria in
activated sludge process. Due to their water
solubility, they are dissolved in water and not being
removed in the sludge which will create problem to
the safety of reclaimed water. Thus, use of RO
process for separation is a key step in the safe
recovery of water from wastewater source .The
recent use of RO in reclamation of wastewater is
done in GWR facility in Orange County for indirect
potable use. It is used to produce 280,000 m
3
/d of
treated wastewater that is used to augment the
groundwater in the region that supplies local
municipalities with drinking water. (Franks 2004). RO
plays an integral role in the advanced treatment
process used at this plant. In this plant, low pressure,
high rejection ESPA2 membranes are used to make
RO permeate with less than 50 mg/l TDS which will
make reclaimed water safe for potential potable
reuse.
Universal Journal of Environmental Research and Technology
237
Garud et al.
2.5 Seawater Reverse:
In SWRO (Sea water Reverse osmosis) unit, the
operating conditions and performance of the HFF
SWRO unit which received the NF product as feed.
The SWRO unit consists of two vessel units, which
are connected in series. During the test period, the
operating pressure was maintained at 60 Kg/cm
2
and
the temperature ranged from 23 to 34
o
C. The
average permeates recovery of the first and second
vessels were around 30 and 21 percent respectively
and the overall recovery of the integrated SWRO
system was about 45%. Chemical analysis revealed
that the majority of the hardness ions and other
dissolved salts were concentrated in the brine reject.
The study revealed that an increase of top Brine
Temperature from 100
0
C to 130
o
C produces 48%
increase in water production. (Hamed, 2005).
3.0 Conclusion:
Feed Water containing suspended particles, organic
matter as well as inorganic salt may deposit on the
membrane and fouling will occur or damage the
membrane because of applied pressure and size of
particles. Therefore the priority to remove these by
way of pretreatment will determine the RO
efficiency. Hence RO membrane performance can be
checked to avoid the irreversible damages to the RO
membrane. In fact success of RO system depends
upon efficiency of the pre treatment. Post treatment
of brine streams present a major problem with
growing desalination capacity to minimize the
damage on the ecology which depends upon the
location of plant.
4.0 Future Scope:
Use of pre-heated feed water, operation at low
pressure, advanced feed water pre-treatment,
advanced energy recovery systems, site specific
optimization and automatic real time plant
management systems are the possible area where
R&D is required with development of membrane
material to sustain maximum temperature which will
increase the productivity of plant thereby reduction
of cost of treatment.
References:
1) Arsuaga, J.M., M.J. Lopez Munoz, A. Sotto and
G. del Rosario, (2006),” Retention of phenols
and carboxylic acids by nanofiltration/reverse
osmosis membranes: Sieving and membrane
solute interaction effects “, Desalination, 731-
733.
2) Bellona, C., J.E. Drewes, P. Xua and G.
Amy,(2004):,”Factors affecting the rejection of
organic solutes during NF/RO treatment-a
literature review, “Water Res., 38: 2795-2809.
3) Bhattacharyya, D., and Madadi, M.R., (1988):
"Separation of Phenolic Compounds by Low
Pressure Composite Membranes: Mathematical
Model and Experimental Results", AIChE
Symposium Series, 84, No. 261, 139.
4) Bhattacharyya, D., Barranger, T., Jevtitch, M.,
and Greenleaf, S., (1987): "Separation of Dilute
Hazardous Organics by Low Pressure Composite
Membranes", EPA Report, EPA/600/87/053.
5) Bodalo-Santoyo, A., J.L. Gomez-Carrasco, E.
Gomez-Gomez, F.Maximo-Martin and A.M.
Hidalgo-Montesinos,(2003):,”Application of
reverse osmosis membrane to reduce pollutants
present in industrial waste water , “Desalination,
155: 101-108.
6) Bodalo-Santoyo, A., J.L. Gomez-Carrasco, E.
Gomez-Gomez, M.F. Maximo-Martin and A.M.
Hidalgo-Montesinos,(2004):”Spiral wound
membrane reverse osmosis and the treatment
of industrial effluents,” Desalination, 160: 151-
158.
7) Chian, E., Bruce, W., and Fang, H., (1975):
"Removal of Pesticides by Reverse Osmosis",
Environmental Science and Technology, 9, 364.
8) Couallier E.M., Ruiz B.S., Lameloise M.L. and
Decloux M., (2006):,” Usefulness of reverse
osmosis in the treatment of condensates arising
from the concentration of distillery
vinasses,”Desalination, 196, 306-317.
9) G. Srinivasan,,S. Sundaramoorthy and D.V.R.
Murthy (2010):,” Spiral Wound Reverse Osmosis
Membranes for the Recovery of Phenol
Compounds-Experimental and Parameter
Estimation Studies,” American J. of Engineering
and Applied Sciences 3 (1): 31-36
10) Koyama, K., Nishi, T., Hashida, I., and Nishimura,
M.,(1982):, "The Rejection of Polar Organic
Solutes in Aqueous Solution by an Interpolymer
Anionic Composite Reverse Osmosis
Membrane", Journal of Applied Polymer Science,
27, 28-45.
11) Krishnan S., Kampman, D., Kumar S. and S.
Nagar, Groundwater and well water quality in
alluvial aquifer of central Gujarat, in Proceedings
of IWMI-Tata Water Policy Programme Annual
Partner’s Meet, Anand, Gujarat,2005
12) Kurihara, M., Harumiya, N., Kanamaru, N.,
Tonomura, T., and Nakasatomi,
M.(1981):”,Development of the PEC-1000
Universal Journal of Environmental Research and Technology
238
Garud et al.
Composite Membrane for Single-Stage Seawater
Desalination and the Concentration of Dilute
Aqueous Solutions Containing Valuable
Materials, “Desalination, 38: 449.
13) Mane J.D., Modi S., Nagawade S., Phadnis S.P.
and Bhandari V.M., (2006): ”,Treatment of
spentwash using modified bagasse and colour
removal studies,” Bioresource Technology, 97,
1752-1755.
14) Mohamed, B., Saida ,B. and Kensa Bensadok
(2006): Groundwater treatment by reverse
osmosis, Desalination, 206: 100–106.
15) Moresi, M., B. Ceccantoni and S. Lo Presti,
(2002):,”Modeling of ammonium fumarate
recovery from model solutions by nanofiltration
and reverse osmosis“, J. Membr. Sci., 209: 405-
420.
16) Murthy,G.V.P, and Choudhari,L.B, (2009):,”
Treatment Of Distillery Spent Wash By
Combined Uf And Ro Processes “,Global NEST
Journal, Vol 11, 2:235-240.
17) Nataraj S.K., Hosamani K.M. and Aminabhavi
T.M., (2006): Distillery wastewater treatment by
the membrane-based nanofiltration and reverse
osmosis processes, Water Research, 40:2349-
2356.
18) Osman A.Hamed, Ata M.Hassan, Khalid Al-Shail
and Mohammed A.Farooque (2005):,
“Performance Analysis Of A Trihybrid
Nf/Ro/MsfDesalination Plant “,International
Desalination Association (IDA) World Congress
Conference held at Singapore in 2005. Osmosis ,
Separation Science and Technology, 22: 745.
19) Pozderivic, A., T. Moslavac and A.
Pichler,(2006):”,Concentration of aqueous
solutions of organic components by reverse
osmosis II. Influence of transmembrane
pressure and membrane type on concentration
of different alcohol solutions by reverse
osmosis, “J. Food Eng., 77: 810-817.
20) Pusch, W., Yu, Y., and Zheng, L., (1989): "Solute-
Solute and Solute-Membrane Interactions in
Hyperfiltration of Binary and Ternary Aqueous
Organic Feed Solutions", Desalination, 75, 3.
21) Ramana S., Biswas A.K. and Singh A.B., (2002):,”
Effect of distillery effluents on some
physiological aspects in maize, “Bioresource
Technology, 84, 295-297.
22) S. Lee, M. Elimelech, C.Booa, S. Honga,
(2010):,” Comparison of fouling behavior in
forward osmosis (FO) and reverse osmosis
(RO)”, Journal of Membrane Science,365, 34–39
23) Schutte, F.C.,(2003):,”The rejection of specific
organic compounds by reverse osmosis
membranes “,Desalination, 158: 285-294.
24) Senthilmurugan, S. and S.K. Gupta,(2006):,”
Separation of inorganic and organic compounds
by using a radial flow hollow fiber reverse
module ,” Desalination, 196: 221-236.
25) Xu, P., J.E. Drewes, C. Bellona, G. Amy and T.U.
Kim et al.,(2005):,” Rejection of Emerging
Organic micro pollutants in nanofiltration-
reverse osmosis membrane applications,” Water
Environ. Res., 77: 40-48.
26) Zhang S., Yang F., Liu Y., Zhang X., Yamada Y. and
Furukawa K., (2006):. Performance of a metallic
membrane bioreactor treating simulated
distillery wastewater at temperatures of 30 to
45 ºC, Desalination, 194, 146-155.
