1. Background

     In a developing world, potable water is a limiting factor for development. Providing drinking water to an increasing population is more complex every year due to the reduction of quality and quantity of surface or ground water or simple geological conditions (such as salt-water intrusion of the water table or desert, dry surface conditions).  Many communities are reaching the limit of what their fresh water resources have to offer. In the Arabian Gulf, water is more valuable than oil and its control often leads to war.  In states like Florida or California, which both have experienced water shortages, water management is an essential issue for growth management.  Alternative sources are necessary to meet the demand for potable water for the future generations.
     Desalination techniques, such as membrane technology, offer one solution to this difficult problem.  By removing contaminants such as salts, heavy metals, radionuclides and pathogens from water of lesser quality, brackish or even saline water can be used to produce potable water.  For the past two decades, the use of a drinking water production technology called reverse osmosis to provide potable water from brackish and saline water sources has increased significantly.

1.1 What is Reverse Osmosis?

     Osmosis is the diffusion flow between two solutions (solvent plus dissolved species or solute) separated by a semi-permeable membrane that only allows the solvent to pass through and acts as a barrier for the solute.  The solvent flows from the medium of lower concentration toward the one of higher concentration (Raven and Johnson, 1991) (Figure 1.1 (a)).  The pressure gradient between the two solutions is called osmotic pressure difference and varies according the concentrations of the solute and the type of solvent present in the two solutions (Figure 1.1 (b)).  Reverse osmosis (RO) is effected when a pressure gradient greater than the osmotic pressure difference is applied on the medium of high concentration.  In this case, the flow is reversed and the solvent travels from high to low concentration areas and the separation of water from solute becomes possible (Bhattacharyya and Williams, 1992) (Figure 1.1 (c)).
 
 

Figure 1.1 Osmosis and Osmotic Pressure.  (a) Solvent flows from the side of low concentration to the one of high concentration.  (b) Before applying osmotic pressure, equilibrium is achieved.  (c) The flow is reversed if a pressure greater than the osmotic pressure is applied on the medium of high concentration. (from Alsaygh, 1991)






     Applying pressure equal or greater than osmotic pressure to a saline solution will reverse the osmotic flow, and potable water will be produced on one side of the membrane while ions and dissolved gas will be concentrated on the other side. Seawater, brackish water or groundwater are treated through RO by using appropriate membranes and can be separated into potable water and concentrate.

1.2  Application of Membrane Technology in Drinking Water Treatment

     Among all the desalination techniques, the RO process allows the production of cleaner drinking water (Pontius, 1996).  Other desalination techniques include NanoFiltration or Membrane Softening (NF or MS), MicroFiltration (MF) and UltraFiltration (UF) and Electrodialysis/Electrodialysis Reversal (ED-EDR).  However, RO remains the Best Available Technology (BAT) according to USEPA (Pontius, 1996) to remove pathogens and most inorganic and organic materials from water (Table 1-1) and is the only desalination process with a filtration size smaller than 1 nm (Table 1-2).
 
 

Table 1-1.  Best available technology (BAT) to remove selected inorganic and radionuclides contaminants from water as well as the removal efficiency achieved for each of them.   (Pontius, 1996)

 
Contaminant BAT Removal Efficiency
(percent)
(inorganics) 
Antimony RO 69-77
Barium RO
EDR
92-98
58-94
Beryllium RO 96-99
Cadmium RO 96-98
Chromium RO 82-97
Cyanide RO 85-99
Fluoride RO 90-95
Mercury RO >80
Nickel RO >90
Nitrate RO
EDR
67-95
51-92
Nitrite RO 67-95
Selenium RO
EDR
75-99
>71
Sulfate RO 86-97
(radionuclides)
Alpha Emitters (proposed) RO 98-99
Beta particles and photon emitters (proposed) RO 90-99
Radium 226 (proposed) RO 87-98
Radium 228 (proposed) RO 87-98
Uranium (proposed) RO 98-99.4
1.2.1 Descriptions of Desalination Processes (Pontius, 1996)
    Several desalination techniques can be used to produce fresh, potable water and include freezing techniques, distillation and membrane technology.  The membrane desalination technologies not only remove the salt content from the salty and brackish water but also provide filtration which increases the quality of the water produced without including the energy costs involved in the thermal methods.
 
 
Table 1-2.  Operating conditions of the most common desalination processes: reverse osmosis (RO), nanofiltration or membrane softening (NF or MS) and electrodialysis/electrodialysis reversal (ED/EDR) (Mickley et al, 1993).
Techniques Feedwater TDS (mg/l) Operating Pressure 
(psi)
Recovery*
(%)
Best for Filtration Size 
(nm)
RO 10,000-45,000
3,500-10,000
500-3,500
high:800-1,200
medium: 600-800
low: 100-600
20-50
60-85
60-85
All 
Type of 
Water
<1
NF or MS 0.0-500 50-150 75-90 Freshwater 1-5
ED-EDR 500-7,500 - 70-95 Brackish Water -
*The recovery is the fraction of potable water obtained from the source water after processing.
 
1.2.1.1 Pressure Driven.
    The basic principle is the same for all pressure driven membrane processes. When pressure greater than the osmotic pressure is applied to a saline solution, osmotic flow through a semi-permeable membrane is reversed and fresh water is produced. The major differences encountered lie in the types of membranes and the operating pressures used by the systems.

Saltwater Reverse Osmosis (SWRO) (high pressure RO) and
Brackish water Reverse Osmosis (BRO) (low and medium pressure RO):
Reverse Osmosis uses a very small pore size membrane and can operate at different pressures according the salinity of the source water.  Brackish surface and groundwater sources are preferred to ocean water due to higher costs for operation and maintenance of SWRO (energy costs for high pressure pumps, maintenance of membranes and pumps degraded by scaling and corrosion).

Membrane Softening (MS) (also known as NanoFiltration) (ultra-low pressure):
Membrane softening operates at much lower pressure due to a membrane more pressure sensitive than the one used in RO plants, and is very effective with groundwater with low Total Dissolved Solids (TDS).

MicroFiltration (MF) and UltraFiltration (UF):
Micro and ultrafiltration use membranes with pore sizes larger than the membranes used by RO and MS.  Consequently, they are not efficient filters for most of the ionic compounds. Micro and ultrafiltration cannot be considered as full desalination techniques, and are only used to clarify the source water.  The water produced by those methods can not be considered potable unless additional post-treatment is applied. MS and UF are not used in the US but represent an interesting research subject.  Most MS and UF plants are found in Europe.  The largest plant is located near Paris, France and has a capacity of 15MGD [57,000 m3/d] (Adham et al, 1996).
 

1.2.1.2 Non-Pressure Driven:
Electrodialysis/Electrodialysis Reversal (ED-EDR):
Electrodialysis and electrodialysis reversal are not pressure driven.  For the ED, an electrical current is passed through the membrane.  The ions will then travel perpendicularly to the membrane (through it), while the water is displaced tangentially.  The EDR is an ED where the current is reversed according to a precise time cycle, allowing periodic flushing of the concentrate and preventing scale or slime formation. EDR is typically used in drinking water treatment while ED is used to treat domestic or industrial wastewater.  However, both are still referred as ED by USEPA regulations.
 
1.2.2 Pre- and Post-Treatment to the Desalination Processes
     The following treatments are part of the process of producing potable water using membrane technology.  Pre-treatment of the feedwater or source water is necessary to remove chemicals such as carbonate or chlorine but also microorganisms, which may cause harm to the system or the membrane itself.  Post-treatments such as chlorination prepare the water for distribution and consumption.  Aeration and degasification are also applied to the concentrate to prepare it for disposal.  The composition of the concentrate will depend on the source water but also the treatment used during processing.  Some of these treatments, their purpose, and their effect on product water and concentrate are shown in Table 1-3.  Most of the chemicals added for pre-treatment will stay in the concentrate.  This is the case for the sulfate from the sulfuric acid used for pH adjustment and from the sodium bisulfite used to decrease chlorine levels that can be harmful for the membrane.  Similarly, the post-treatments affect the concentrate composition.  The presence of chlorine in the concentrate comes from desinfection of the desalination by-product before discharge.  The aeration used to remove dissolved gases from the concentrate will oxidize hydrogen sulfide and ammonia into sulfate and nitrate and increase dissolved oxygen concentration.  Moreover, the sodium level of the concentrate may be raised by using sodium hydroxide for pH adjustment.
 
 
Table 1-3. A summary of pre- (a) and post- (b) treatment processes employed during  potable water production by desalination (Mickley et al, 1993).
(a) Pre-treatment step Purpose Chemicals Added Fate of Chemicals
pH Adjustment to 7  Decrease Carbonate Concentration (and Carbonate Precipitation), Protect Membrane from Hydrolysis Acid (H2SO4) Affect pH of both produced water and concentrate, sulfate stays in the concentrate
Antiscalants  Prevent Formation of Scalling on the Membranes Sequestering Agent, dispersants  Complexes formed stay in concentrate
Coagulation-filtration  Prevent Fouling and Clogging of the Membranes  Coagulants-flocculants  Flocullants formed settle out and are removed by filtration
Desinfection  Prevent Biological Fouling and Remove Microorganisms that feed on Membranes Material  Chlorine (or Biocides, UV)  Chlorine distributed equally in permeate and concentrate
Dechlorination  Protect Chlorine-Sensitive Membranes  Sodium Bisulfite or Granular Activated Carbon (GAC)  Reacts with Chlorine to form sulfate and chloride that stay in concentrate
(b) Post-treatment step Purpose Chemicals Added or Method Used Fate of Chemicals
Remove Dissolved Gases  Remove Objectionnable Gases, CO2, Radon and H2S Aeration, Degasification  Oxydize H2S and NH4 in both produced water and concentrate
pH Adjustment to 7  Prevent Corrosion in Distribution System, Protect Aquatic Life in case of Surface Discharge NaOH, soda ash, lime  Increase sodium level in both produced water and concentrate
Desinfection  Prevent Bacterial Growth in Distribution System, Protect Aquatic Life if necessary  Chlorine (or Chloramination)  Chlorine stays in produced water and concentrate
Reduction of Chlorine Level  Eliminate Chlorine and other Oxidizers Sodium Bisulfite or GAC Increase sulfate and chloride levels in both produced water and concentrate if necessary
Oxygenation Increase Dissolved Oxygen to Level Supporting Aquatic Life Aeration Increase DO in Concentrate
Remove Other Species Decrease any Pollutants that may be present in Produced Water and Concentrate Depends on Species

1.3  Concentrate Disposal

    Worldwide, desalination plants use RO more than any other desalination process to treat seawater as well as brackish and fresh water (AWWA-MTRC, 1998).  In Florida, the production of potable water from brackish groundwater by RO has increased exponentially for the past three decades (Figure 1.2). If the impacts on surface and groundwater supplies due to the pumping of increased amounts of water to be treated can be minimized, the major concern of the application of RO is for concentrate disposal.
 
 

Figure 1.2 Production of potable water by desalination processes compared to Florida population growth (University of South Florida, 1998).


1.3.1 What is the problem?
         Concentrate from potable water production by desalination is considered by the public to be a brine, a hypersaline solution several times more concentrated than seawater.  Actually, desalination by-product is concentrated source water with a chemical  composition similar to the source water (with the exception of a few chemicals added during post and pre-treatments of the desalination process) but with concentrations 2 to 5 times higher than the source water.  The concentrations of chemical species of the groundwater and surface water used as feed water by membrane processes depend on a variety of different factors such as the geology of the terrain or the rainfall in the area and vary greatly from one place to an other.  The concentrates obtained from those feed waters present great variations from one to another as can be seen in Table 1-4.  For example, chloride can be found in desalination by-product in concentrations ranging from 100 mg/l to 30,000 mg/l according to the total dissolved solids (TDS) content of the feed water. Therefore, there are as many different concentrates as there are feed waters.  However, the concentrate is classified as an industrial waste, which may be toxic to aquatic life (http://www.dep.state.fl.us/-ned/wfweb/pages/industri.htm).
 
1.3.1.1 Why is concentrate classified as an industrial waste? Of what consequence is this classification for the disposal of concentrate?
     Wastewater is classified by USEPA into five categories (40 CFR 35); each characterized by the absence or presence of coliform bacteria, or whether the waste stream results from agricultural activities, stormwater, thermal processes with temperature gradient, or industrial processes.  Desalination concentrate was designated as industrial waste, a classification with more stringent regulations than domestic waste.  These more stringent requirements have affected the use of reverse osmosis in the US.
 
 
Table 1-4 Inventory and typical values of the chemical species found in desalination concentrate.
Major Ions and Constituents of Concentrate  Origin  Level in Concentrate (mg/l)* USEPA Standards (mg/l)
Chloride Source Water/Desinfection Process  100-30,000  <10%  above the background value
Sodium Source Water/pH adjustment 50-20,000 report**
Sulfate Source Water/Dechlorination 200-4,000 500
Magnesium Source Water 30-2,000 report**
Calcium  Source Water  250-1,000 report**
Bicarbonate Source Water -  
Potasium Source Water 10-500 report**
Fluoride Source Water 0.5-10 5
Iron Source Water - report**
Ammonia Source Water -  
Hydrogen Sulfide***  Source Water 0.01-1 0.02
Carbon Dioxide*** Source Water -  
Dissolved Oxygen Added during Aeration of the concentrate before Discharge  0.5-10  > 5.0
Radon Source Water 5-50 pCi/l 20 pCi/l
* From FDEP 1993
** FDEP monitoring requirements
*** Can be removed during Aeration of the concentrate before discharge
 
1.3.1.2 Ion imbalance and toxicity.
 The production of concentrate does not include adding toxic chemicals, but only the removal of water from the source water.   Often, the concentrations of materials found in the concentrate are below USEPA water quality standards.  However, concentrates from several desalination plants have been found acutely and chronically toxic to aquatic life in a variety of bioassays performed by FDEP (http://www.dep.state.fl.us/labs/biol/BSSYmap.html).  In addition, heavy metal contamination of sediments in the vicinity of concentrate discharge pipes from a Saudi Arabia SWRO water treatment plant has been documented in one non-peered reviewed publication (Sadiq, 1995).  The increased concentration of fluoride, ammonium, heavy metals and/or radionuclides and dissolved gases such as H2S or CO2 can reach toxic levels, above USEPA maximum contamination levels (MCL), and cause mortality in organisms. The MCL is the minimum concentration that may be released in the environment before harmful effects occur.  For example, the MCL for fluoride is 5mg/l according to USEPA, but fluoride has been found with concentration as high as 9.8 mg/l in the concentrate from the Jupiter RO plant in October 1994 (http://www.dep.state.fl.us/labs/biol/Report_Smmrys/-BSSY_Smmrys/CEdist/) while the fluoride levels of the Melbourne RO plant never got over 2 mg/l in three years of operation (Appendix A:  Melbourne ROWTP NPDES monitoring results).  Moreover, an imbalance in the ratios of major ions when compared to seawater has been observed frequently in concentrate derived from groundwater sources.
 The major sea ions (chloride, sodium, sulfate, calcium magnesium, potassium, and bicarbonate) present a conservative behavior in estuarine waters and seawater (Berner and Berner, 1996).  This means that even if their concentrations change, the ratios comparing one to another stay constant at any location in those waters.  This is not true for the groundwater used by membrane plants and the major sea ions in brackish groundwater (and hence, in concentrate from groundwater) do not behave conservatively. Imbalance in the ratio of the major seawater ions has been discovered to have a negative synergistic effect on marine life that could lead to mortalities (FDEP, 1993).
 If the concentrate is proven toxic for aquatic life and fails bioassays, it is important to determine the cause in order to address the specific toxicant.  As an example, removal of H2S and CO2 by aeration prior to discharge have become a routine post-treatment practice in most of the US to address toxicity and corrosivity from these substances.
 
1.3.2 What to do with the concentrate?
Several alternatives are available for the disposal of the desalination by-product.  The concentrate can be discharged to an adjacent surface water body or to a municipal sewer system, injected into a deep well, reused for land application or converted to solid waste.  Here is a description of each of those options.
 
1.3.2.1 Dilution in surface water.
 Discharging the concentrate into surface water is the most common method of concentrate disposal in the world and is the least expensive alternative (Mickley 1993).  In the US, the Clean Water Act (1977) (USC 33 s/s 121 et seq.) states that the disposal of any effluent in surface water requires a National Pollutant Discharge Elimination System (NPDES) permit (40 CFR 122) (http://www.epa.gov/epahome/laws.htm).  Discharges are allowed if the contaminants in the effluent meet certain standards set by USEPA (40 CFR 122.41-45), state or local environmental protection agencies (40 CFR 123.25).  NPDES permits require extensive monitoring to include background conditions, effluent quality, and effluent toxicity.  Recent concerns about concentrate toxicity have made discharge to surface water unpopular with the public (Florida Today, April 14th 1999).
1.3.2.2  Deep Well Injection (DWI)
 The wastewater is injected into a deep well, typically four hundred meters below the aquifer or any underground source of water present at the location of the well.  Injection wells are used to dispose of a variety of liquid wastes ranging from domestic wastewater to hazardous material.  This technique has been found to be safe by USEPA provided the material stays in the injection zone and operators respect regulations (42 USC s/s 300h).
 A good understanding of the hydrogeology of the area and the sub-surface geology are required if DWI is to be used. Injection is not possible everywhere.  The geological formation designated for wastewater disposal must have a confining layer and prevent horizontal and vertical migration of the wastewater.  Vertical or horizontal migration may occur when the system is not operated or designed correctly.  Poor system operation may promote corrosion of the injection module or an excessive injection pressure and poor designs may result in leaks in the casing or may fail to determine that the confining beds are permeable or include faults or fractures.  This may lead to contamination of the adjacent aquifer.
 Underground Injection Control (UIC) program (40 CFR 144) establishes minimum federal standards and engineering designs for deep wells, which are grouped into five different classes, each class corresponding to a very well defined type of waste or operation (Table 1-5).
 
 
Table 1-5.  Deep injection wells for waste disposal as classified by the Underground Injection Control program (40 CFR 144.6).
Class I  Domestic and Hazardous Waste
(municipal wells)
Class II  Waste from Oil Industries
Class III  Waste from Mining Industries
Class IV Radioactive Materials
Class V All the other wastes (Septic Waste, Stormwater, Brine and Concentrate)

     Concentrate is an industrial waste but has not been included in the list of hazardous waste that can be injected in Class I wells.  Desalination by-product requires a Class V well for deep well disposal.  The costs associated with upgrading a Class I municipal well to a Class V well may limit the use of DWI for disposal of concentrate.  In addition, the environmental consequences of deep well injection are not completely understood and require further investigations.

1.3.2.3 Sewage treatment or Publicly Owned Treatment Work (POTW).
     Discharging the concentrate to a municipal sewer system has the potential to be a good solution.  Costs may be lower than the other method of disposal because wastewater treatment plant already exists.  When concentrate and domestic water are mixed, both are diluted.  The fecal coliform count of the domestic wastewater is reduced with the addition pathogen-free concentrate and the salt content of the concentrate is reduced by the dilution of fresh domestic wastewater.  In addition, the overall toxicity of the blend may also be reduced.  On the other hand, the volume of the concentrate may be greater than the treatment capacity of the POTW and may require a development of the facility.
1.3.2.4 Land application (Evaporation ponds and irrigation).
     Evaporation ponds have been used to store the concentrate, reduce its water content and dispose of the sludge as a solid waste. The pond must be designed to be leakproof to prevent groundwater contamination and, of course, evaporation pond applications are only possible in locations where the evaporation rates (usually measured in gallons/day/acre) are sufficiently high to promote rapid evaporation.  Finally, the costs for this method include land acquisition, dredging, and sludge disposal.
 Irrigation is another type of land application.  This alternative requires soils with sufficient absorption rate (measured in ft/year), a good rainwater flushing and often an aeration pond for storage before spraying.  Typical absorption rates varies between few tenth of ft/year to 20 to 30 ft/year.  Spray irrigation may not be a feasible alternative if concentrations of chlorides or other materials present a threat to local aquifers.  In addition, the tolerance of the crops or other vegetation to chlorides and other constituents of the concentrate must be considered.  Irrigation is a good solutions for small capacity plants with low salt content concentrate.
1.3.2.5  Water minimization
     Some plant operators propose to transform the concentrate into solid waste by evaporating all of its water content through crystallization and heat transfer.  The concentrate is compressed and boiled to lower its water content.  The efficiency of such system is measured with its percent rejection.  The percent rejection is the percentage of the final volume of brine compared to the initial volume of concentrate. This method requires high-energy cost to provide evaporation heat, a major capital investment and the availability of a landfill designed to hold the waste products.
 
 

     According to Mickley (1993), the solution to concentrate disposal other than surface discharge that answers the best any financial and environmental concerns lies in deep well injection (when the hydrogeology allows it) for large capacity plants (>0.5MGD [>1,900 m3]) and in land application (spraying) for smaller units (Table 1-6).
 
 

Table 1-6  Comparative costs for non-surface discharge concentrate disposal options as a function of flow rate in thousands of dollars (1992) (Mickley et al., 1993)
Flow rate Evaporation Ponds Deep Well Spray Irrigation Brine Concentrator
(MGD) 750 GD/acre 3,000 GD/acre 2,500 ft 10,000 ft 2 ft/yr 20 ft/yr 2% rejection 10% rejection
0.01 806 276 663 1,705 154 41 1,812 2,078
0.1 6,672 1,794 663 1,705 984 204 3,086 3,730
1 66,720 17,940 927 2,300 8,286 1,272 15,740 19,230

    Recently, the city of Melbourne has reviewed the costs associated with three different alternatives for disposal of concentrate from their RO facility which presently  discharges to the Eau Gallie River.  The cost of a deep well injection solution were ranging from 3.5 to 10 millions dollars while displacing the point of discharge from the creek to the Indian River Lagoon was estimated to cost $1 million (A final alternative considered by the city involved an ocean outfall with an estimated cost of $4 millions).
    Membrane technology is a relatively new technology developed industrially for only two decades.  Much information about the possible toxicity remains to be thoroughly investigated.  As an example, seawater ion imbalance as a cause of toxicity for aquatic organisms has only recently been discovered.  Similarly, little is known about the effects of disposal methods.
 


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