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Total organic carbon feed water

The slurry effluent is analyzed for residual organics, and if it meets total organic carbon (TOC) specifications, it is pumped to an evaporator/crystallizer system, where water is evaporated and the salts crystallized for off-site disposal. These inorganic salts are readily stabilized and are suitable for disposal in existing permitted landfills. The recovered water is either reused in the process, sent to a unit that produces deionized water, or used for making caustic solution. If the effluent does not meet TOC specifications, it is routed to an off-specification effluent tank and then returned as part of the SCWO reactor feed. [Pg.101]

The Feed analysis screen is reached via the menu under "Tools— Input—Water Analysis," or by the "HzO" button at the top of the main screen. Up to three feed analyses can be entered. Concentration can be entered as ppm ion, ppm as calcium carbonate, or as milli-equivalence per liter. Standard species, such as calcium and sodium, are entered. There is also space for four designer-defined species of interest. Examples of designer-defined species include total organic carbon, boron, and the like. Note that the program will not automatically calculate permeate and concentrate concentrations for these designer-defined species. [Pg.231]

Other Reported Studies Brady [105] has reported on UF systems (start-up 2000) for mill water recovery and reuse. The Koch tubular HFP-276 (PVDF) membrane used removes 50% of COD, TDS, and total organic carbon (TOC). The UF operating cost is 1.6 per cubic meter. The plant operates continuously atarecovery rate of 98.7%. The feed stream and the null are not reported. [Pg.995]

L/min and up to 18.3 megohm-cm water with less than 10 ppb total organic carbon content. Use a three-module system for tap feed water, and a four-module system for high purity quality tap water. [Pg.275]

To determine the organic rejection by the FO process, the total organic carbon (TOC) concentration was measured. The initial TOC concentration in the feed was 130 mg/L and the final concentration (after approximate 50% volnme reduction) was 235 mg/L. The TOC concentration in the draw solution was less than 1 mg/L this indicates that the FO membrane can effectively reject the organics in the feed water. Table 1 shows the concentration for the anions and cations present in the feed and draw solutions. [Pg.314]

Where c, and are the concentrations of chloroform or monochloroacetic acid in the permeate, in the feed and the base concentration of the de-ionized (DI) water, respectively. Chloroform concentrations were determined using a total organic carbon (TOC) analyzer using the UV-persulfate method (Phoenix 8000, Rosemount Analytical Inc., Tekmar Dohrmann Division, Santa Clara, CA). Concentration of monochloroacetic acid was determined using a conductivity/TDS meter with RS232C (CON 110 series, Oakton Instruments, Vernon Hills, IL, manufactured by Eutech Instruments, Singapore). [Pg.192]

As organisms feed, they convert some organic matter and nutrients into biomass of their own bodies, while another portion is excreted as waste from respiration. Therefore, as food chains proceed toward completion, the amount of biomass may be totally reduced through metabolic processes to carbon dioxide, water, and several mineral nutrients that remain in solution. [Pg.278]

The total per-pa s yields of anhydrous oxygenated organic product per gallon of pentane is about 0.151 pounds or about 0.0285 pounds per pound of entering pentane. This should be contrasted with the yields obtained in the case of the oxidation of aromatic hydrocarbons where complete oxidation of entering hydrocarbon to either product or water and carbon dioxide is aimed at. In the absence of data on the amount of destructive oxidation of the pentane no comparison of the heat evolution in the two cases is possible although it is safe to say that in the case of pentane the amount of heat evolved per unit of feed is much less than in the case of the aromatics because of the restricted amount of oxygen present in the former case. [Pg.203]

D-(+)-Biotin (1), a biocatalyst of reversible metabolic reactions of carbon dioxide transport in organisms, is one of the water-solnble B-complex gronp of vitamins and has immense commercial importance in ponltry feeds and animal nntrition. Componnd 1 was isolated from egg yolk, liver and milk concentrates. " It is an important vitamin for human nutrition and animal health. " Its structure was determined and confirmed by the first total synthesis. Its absolute configuration by X-ray crystallographic analysis was established. Syntheses of biotin from noncarbohydrate and its analogues from carbohydrate and noncarbohydrate have been reported. " Syntheses from carbohydrate precursors are discussed in this part. [Pg.300]


See other pages where Total organic carbon feed water is mentioned: [Pg.454]    [Pg.6]    [Pg.265]    [Pg.377]    [Pg.163]    [Pg.314]    [Pg.410]    [Pg.104]    [Pg.28]    [Pg.172]    [Pg.107]    [Pg.50]    [Pg.582]    [Pg.653]    [Pg.2952]    [Pg.38]    [Pg.582]    [Pg.386]    [Pg.286]    [Pg.341]    [Pg.621]    [Pg.52]    [Pg.749]    [Pg.52]   
See also in sourсe #XX -- [ Pg.273 ]




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Carbonated waters

Feed organizer

Total carbon

Total organic carbon

Water carbon)

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