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Storage of Salt

Standpoint this is an inferior process. More frequently, the salt is in intermediate storage and must be moved as the solid to a dissolver. This involves the use of mobile equipment that generally is equipped to break up a crusty surface as well as to lift the salt. [Pg.493]

Any loss of salt from a pile must be regarded as a form of pollution. Salt, however, is quite benign and is not deemed a serious pollutant. Handling of solid salt, especially in windy conditions, produces a fine dust. This drift is one consideration in siting a salt storage pile. The wind-blown salt can be a nuisance in process areas and usually ends up in the plant s effluent water system. Salt dissolved from the pile (e.g., by rainfall) can be recovered by collection in a sump and returned to the process. [Pg.493]

Salt is also lost in rainwater runoff. Crusting of the surface of the pile by accumulation of insolubles actually helps to limit this loss. The storage pad should be sloped at least 1-2% to remove drainage to a catchment efficiently and to prevent accumulation of surface water [29]. At the same time, the slope should be limited to about 5% [30], above which operation of equipment like front-end loaders can become unstable. On large pads, ditches and pipes can improve drainage. The drainage should be away from any adjacent ground-water system. Otherwise, it can follow the terrain. [Pg.493]

At the chlor-alkali plant, storage usually is in conical piles or windrows. The volume of a cone is one third that of a cylinder with the same diameter and height. The height of the cone in this case is related to its diameter by the angle of repose of the salt  [Pg.493]

6 = base angle (assumed equal to angle of repose) [Pg.493]


It was once thought that the saltiness of the modem oceans simply represents the storage of salts derived from rock weathering and transported to the oceans by fluvial processes. With increasing knowledge of the age of the earth, however, it was soon realized that, at today s rate of delivery of salt to the ocean or even at much reduced rates, the total salt content and the mass of individual salts in the... [Pg.592]

Figure 10 The dryland salinization cycle (the Australian model) (1) salt accumulation and precipitation of minerals (2) selective dissolution and transport of soluble salts in the vadoze zone (3) storage of salts influenced by soil permeability (4) leaching and salinization of groundwater (5) rise of saline groundwater (6) capillarity evaporation of rising groundwater (7) soil salinization and (8) lateral solute transport and salinization of streams and rivers (after Fitzpatrick et ah, 2000). Figure 10 The dryland salinization cycle (the Australian model) (1) salt accumulation and precipitation of minerals (2) selective dissolution and transport of soluble salts in the vadoze zone (3) storage of salts influenced by soil permeability (4) leaching and salinization of groundwater (5) rise of saline groundwater (6) capillarity evaporation of rising groundwater (7) soil salinization and (8) lateral solute transport and salinization of streams and rivers (after Fitzpatrick et ah, 2000).
This paper mentions the various modes now being considered for long-term storage of salt cake and encapsulated fission products. Processes to increase immobilization of the stored high-level waste are currently being developed status of the development work on these processes is also reviewed. [Pg.55]

Plant design must also cater to the shutdown of one line of cells. If the diaphragm cells are shut down, the mercury cells can operate on stockpiled evaporator salt or purchased salt. If neither is available, the mercury cells will be forced to shut down. In the case of a mercury-cell shutdown while evaporator salt is still being produced, the salt can be stockpiled in a resatmator (see Section 1.22.2 for a discussion on wet storage of salt) or used to produce new brine. The latter approach probably involves curtailment of production from the diaphragm cells. [Pg.996]

Hydroxjiamine is used as a substitute for the ferrous sulfamate (26). These systems are called salt-free flow sheets. The main purpose is to ease the problems associated with the processing and storage of the Hquid waste streams (27). Another approach is to use an electropulse column to electrolyticaHy produce to reduce Pu to Pu on a continuous basis (28,29). The half reactions for the flow sheets are... [Pg.205]

An environmental risk in solution mining is surface subsidence. This risk is greatest with embedded salt. No cases of salt subsidence have been reported in mining domes that have been mined according to standard industry approved practice in the United States, but some have been seen in other countries. One side benefit of dome solution mining is use of the cavities later for storage of industrial fluids, chiefly petroleum and natural gas. [Pg.409]

There is no difficulty in handling or storage of corrosive chemicals or effluents. Salt is easily purchased and handled in bulk, and can be discharged directly into a standard commercial salt saturator. [Pg.481]

Blood and lymph are approximately isotonic to a cell so that cells do not gain or lose liquid when bathed in these fluids. Pure water is hypotonic and may cause cells to swell and burst. During intravenous feeding, injections, and storage of cell tissue, a salt (saline) solution is used with a concentration of solutes that is essentially isotonic with blood (and hence, with the cell) to prevent cell damage. [Pg.374]

Salts of a-sulfo fatty acid esters can work as emulsifying agents for the preparation of asphalt emulsions and asphalt-latex emulsions. The ester sulfonates improve the storage stability of the emulsions [101,102]. In the manufacture of lightweight gypsum products air bubbles have to be mixed into the slurries. The use of salts of sulfonated C10 l8 fatty acid alkyl esters as foaming agents produces uniformly distributed fine bubbles [103]. Salts of C10 16 fatty acid alkyl ester sulfonates can also be added to cement mixtures to prevent slump loss of the mixtures [104]. [Pg.491]

G J. Janz, C. B. Allen, N. P. Bansal, R. M. Murphy, and R. P. T. Tomkins, Physical Properties Data Compilations Relevant to Energy Storage, Molten Salts Data on Single and Multi-Component Salt Systems, U.S. Dept, of Commerce, National Bureau of Standards, NBS-NSRDS-61, Washington, DC, 1979. [Pg.198]

Depending on the composition of the active materials and on the manganese dioxide type employed, the OCV of freshly manufactured zinc-carbon cells with salt electrolyte varies between 1.55 and 1.85 V. It decreases during discharge and formation of the variable-composition mass. Upon prolonged storage of undischarged batteries, their OCV also decreases. [Pg.351]


See other pages where Storage of Salt is mentioned: [Pg.59]    [Pg.60]    [Pg.492]    [Pg.59]    [Pg.60]    [Pg.492]    [Pg.186]    [Pg.232]    [Pg.275]    [Pg.451]    [Pg.185]    [Pg.472]    [Pg.491]    [Pg.444]    [Pg.471]    [Pg.471]    [Pg.1019]    [Pg.347]    [Pg.1257]    [Pg.1056]    [Pg.153]    [Pg.99]    [Pg.180]    [Pg.451]    [Pg.464]    [Pg.501]    [Pg.190]    [Pg.10]    [Pg.429]    [Pg.248]    [Pg.43]    [Pg.1678]    [Pg.1744]    [Pg.98]    [Pg.394]    [Pg.591]    [Pg.53]    [Pg.539]    [Pg.1650]    [Pg.45]   


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Salt storage

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