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Brackish

Gr. iodes, violet) Discovered by Courtois in 1811, Iodine, a halogen, occurs sparingly in the form of iodides in sea water from which it is assimilated by seaweeds, in Chilean saltpeter and nitrate-bearing earth, known as caliche in brines from old sea deposits, and in brackish waters from oil and salt wells. [Pg.122]

Silver reduces the oxygen evolution potential at the anode, which reduces the rate of corrosion and decreases lead contamination of the cathode. Lead—antimony—silver alloy anodes are used for the production of thin copper foil for use in electronics. Lead—silver (2 wt %), lead—silver (1 wt %)—tin (1 wt %), and lead—antimony (6 wt %)—silver (1—2 wt %) alloys ate used as anodes in cathodic protection of steel pipes and stmctures in fresh, brackish, or seawater. The lead dioxide layer is not only conductive, but also resists decomposition in chloride environments. Silver-free alloys rapidly become passivated and scale badly in seawater. Silver is also added to the positive grids of lead—acid batteries in small amounts (0.005—0.05 wt %) to reduce the rate of corrosion. [Pg.61]

In reverse osmosis membranes, the pores are so smaH, in the range 0.5— 2 nm in diameter, that they ate within the range of the thermal motion of the polymer chains. The most widely accepted theory of reverse osmosis transport considers the membrane to have no permanent pores at aH. Reverse osmosis membranes are used to separate dissolved microsolutes, such as salt, from water. The principal appHcation of reverse osmosis is the production of drinking water from brackish groundwater or seawater. Figure 25 shows the range of appHcabHity of reverse osmosis, ultrafiltration, microfiltration, and conventional filtration. [Pg.75]

The fourth fully developed membrane process is electrodialysis, in which charged membranes are used to separate ions from aqueous solutions under the driving force of an electrical potential difference. The process utilizes an electrodialysis stack, built on the plate-and-frame principle, containing several hundred individual cells formed by a pair of anion- and cation-exchange membranes. The principal current appHcation of electrodialysis is the desalting of brackish groundwater. However, industrial use of the process in the food industry, for example to deionize cheese whey, is growing, as is its use in poUution-control appHcations. [Pg.76]

The first reverse osmosis modules made from cellulose diacetate had a salt rejection of approximately 97—98%. This was enough to produce potable water (ie, water containing less than 500 ppm salt) from brackish water sources, but was not enough to desalinate seawater efficiently. In the 1970s, interfacial composite membranes with salt rejections greater than 99.5% were developed, making seawater desalination possible (29,30) a number of large plants are in operation worldwide. [Pg.80]

Although the principal appHcation of reverse osmosis membranes is still desalination of brackish water or seawater to provide drinking water, a significant market is production of ultrapure water. Such water is used in steam boilers or in the electronics industry, where huge amounts of extremely pure water with a total salt concentration significantly below 1 ppm are required to wash siUcon wafers. [Pg.81]

Electro dialysis is used widely to desalinate brackish water, but this is by no means its only significant appHcation. In Japan, which has no readily available natural salt brines, electro dialysis is used to concentrate salt from seawater. The process is also used in the food industry to deionize cheese whey, and in a number of poUution-control appHcations. [Pg.82]

Desalination. Desalination of seawater and brackish water has been and, as of the mid-1990s, is the primary use of RO. Driven by a need for potable water in areas of the world where there is a shortage, this industry has developed. Desalination involves the reduction of the total dissolved soHds (IDS) concentration to less than 200 mg/L. RO offers several advantages over other possible desalination processes such as distillation (qv), evaporation (qv), and electro dialysis. The primary advantage of RO over the traditionally used method of distillation is the energy savings that is afforded by the lack of a phase change in RO. [Pg.154]

Reverse osmosis processes for desalination were first appHed to brackish water, which has a lower I DS concentration than seawater. Brackish water has less than 10,000 mg/L IDS seawater contains greater than 30,000 mg/L IDS. This difference in IDS translates into a substantial difference in osmotic pressure and thus the RO operating pressure required to achieve separation. The need to process feed streams containing larger amounts of dissolved soHds led to the development of RO membranes capable of operating at pressures approaching 10.3 MFa (1500 psi). Desalination plants around the world process both brackish water and seawater (15). [Pg.154]

In oil and gas refinery appHcations, titanium is used as protection in environments of H2S, SO2, CO2, NH, caustic solutions, steam, and cooling water. It is used in heat-exchanger condensers for the fractional condensation of cmde hydrocarbons, NH, propane, and desulfurization products using seawater or brackish water for cooling. [Pg.110]

Some inland municipalities now distribute water with salt content exceeding 1000 ppm, water so brackish as to be unpleasant to the taste, even though it is distributed as potable water. Each home may produce or purchase the very small requirement of freshwater for drinking and cooking. Small... [Pg.237]

Water in Industry. Freshwater for industry can often be replaced by saline or brackish water, usually after sedimentation, filtration, and chlorination (electrical or chemical), or other treatments (22). Such treatment is not necessary for the largest user of water, the electric power industry, which in the United States passed through its heat exchangers in 1990 about 40% of the total supply of surface water, a quantity similar to that used for agriculture, and it was 48% of the combined fresh and saline water withdrawals (10). Single stations of 1000 MW may heat as much as 12 Mm /d by as much as 10—15°C. [Pg.238]

The pressure to be used for reverse osmosis depends on the salinity of the feedwater, the type of membrane, and the desired product purity. It ranges from about 1.5 MPa for low feed concentrations or high flux membranes, through 2.5—4 MPa for brackish waters, and to 6—8.4 MPa for seawater desalination. In desalination of brackish or sea water, typical product water fluxes through spiral-wound membranes are about 600—800 kg/m /d at a recovery ratio RR of 15% and an average salt rejection of 99.5%, where... [Pg.250]

The plant scheme shown in Figure 14a is generally used in brackish-water conversion that in Figure 14b is utilized in seawater-conversion plants. [Pg.250]

Fig. 15. Ion movements in the electro dialysis process. Courtesy U.S. Agency for International Development, (a) Many of the substances which make up the total dissolved soHds in brackish water are strong electrolytes. When dissolved in water, they ionize ie, the compounds dissociate into ions which carry an electric charge. Typical of the ions in brackish water are Cl ,, HCO3, , and. These ions tend to attract the dipolar water molecules... Fig. 15. Ion movements in the electro dialysis process. Courtesy U.S. Agency for International Development, (a) Many of the substances which make up the total dissolved soHds in brackish water are strong electrolytes. When dissolved in water, they ionize ie, the compounds dissociate into ions which carry an electric charge. Typical of the ions in brackish water are Cl ,, HCO3, , and. These ions tend to attract the dipolar water molecules...
The voltage used for electro dialysis is about 1 V per membrane pair, and the current flux is of the order of 100 A/m of membrane surface. The total power requirement increases with the feedwater salt concentration, amounting to about 10 MW per m product water per 1000 ppm reduction in salinity. About half this power is required for separation and half for pumping. Many plant flow arrangements exist, and their description can be found, along with other details about the process, in References 68 and 69. Many ED plants, as large as 15,000 vsf jd, are in operation, reducing brackish water concentration typically by a factor of 3—4. [Pg.253]

A notable example of controlled water reuse was utilization of secondary sewage effluent from the Back River Wastewater Treatment Plant in Baltimore by the Sparrows Point Works of Bethlehem Steel (6). The Sparrows Point plant was suppHed primarily by weUs located near the brackish waters of Baltimore harbor. Increased draft on the weUs had led to saltwater intmsion. Water with chloride concentration as high as 10 mg/L is unsuitable for many steelmaking operations. Rollers, for example, are pitted by such waters. However, treated effluent from the Back River Plant can be used for some operations, such as coke quenching, and >4 x 10 m /d (10 gal/d) are piped 13 km to Sparrows Point. This arrangement has proved economical to both parties for >40 yr. [Pg.291]

Marine borers inhabit saline or brackish waters where they cause serious destmction to untreated wood. The moUusks include the Teredo and Bankia borers among the cmstaceans, the Limnoria borers are the most widespread and destmctive. Preservatives or borer-resistant woods deter marine borers (see Coatmgs, marine). [Pg.329]

Cellulose acetate films, specially cast to have a dense surface and a porous substmcture, are used in reverse osmosis to purify brackish water (138—141) in hollow fibers for purification of blood (artificial kidney) (142), and for purifying fmit juices (143,144) (see Membrane technology). [Pg.259]

Diatoms inhabit fresh, brackish, or sea waters. Environmental changes ia the bodies of water where diatoms flourish are reflected by the different types of diatoms that may appear at different levels of the same deposit. [Pg.56]


See other pages where Brackish is mentioned: [Pg.12]    [Pg.35]    [Pg.150]    [Pg.152]    [Pg.153]    [Pg.154]    [Pg.154]    [Pg.74]    [Pg.303]    [Pg.144]    [Pg.145]    [Pg.154]    [Pg.154]    [Pg.156]    [Pg.156]    [Pg.156]    [Pg.102]    [Pg.110]    [Pg.237]    [Pg.238]    [Pg.238]    [Pg.239]    [Pg.240]    [Pg.240]    [Pg.255]    [Pg.321]    [Pg.55]    [Pg.151]    [Pg.175]    [Pg.175]    [Pg.175]   
See also in sourсe #XX -- [ Pg.561 ]

See also in sourсe #XX -- [ Pg.6 , Pg.7 , Pg.11 , Pg.18 , Pg.19 , Pg.20 , Pg.25 , Pg.32 , Pg.38 , Pg.287 , Pg.288 , Pg.330 , Pg.361 , Pg.447 , Pg.448 , Pg.483 , Pg.486 , Pg.489 , Pg.518 , Pg.525 , Pg.544 , Pg.566 , Pg.587 , Pg.600 , Pg.605 , Pg.626 , Pg.629 ]

See also in sourсe #XX -- [ Pg.144 , Pg.197 ]

See also in sourсe #XX -- [ Pg.561 ]




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Algae brackish water

Brackish and seawater desalination

Brackish conditions

Brackish marsh

Brackish outflow

Brackish surface water

Brackish water

Brackish water RO

Brackish water desalination

Brackish water desalination systems integration

Brackish water membranes

Brackish water membranes high-productivity membrane

Brackish water membranes membrane modules

Brackish water membranes modules

Brackish water membranes test conditions

Brackish water usage

Brackish water, definition

Desalination of brackish water

Electrodialysis brackish water desalination

Electrodialysis performance, brackish water

Environment brackish

From fresh and brackish water

Membrane scaling brackish waters

Membranes brackish water desalination

Natural waters brackish water

Performance, brackish water

Phytoplankton brackish

Production of Freshwater from Seawater and Brackish Water

Reverse osmosis brackish water

Reverse osmosis brackish water desalination

Reverse osmosis membrane brackish water desalination

Total Desalination of Brackish Water

Water, acid brackish

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