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Water temperature range

The effectiveness of chlorine residuals increase with higher temperatures within the normal water temperature range. [Pg.48]

NOTE Dual-temperature systems provide both HW and chilled water functions and employ common piping for much of the system. Water temperatures range from 34 °F/1.1 °C up to perhaps 250 °F/121.1 °C. [Pg.394]

Also, Amie and Alberto [22] obtained good correlations between mean annual water temperatures, mean annual water temperature ranges and heights for the rivers of the Ebro River basin. Comparing the actual water temperature with the estimated water temperature they observed that some rivers (rivers Jalon, Jiloca, Martin) showed higher temperatures than expected. However, although the authors formulated some hypothesis for such alterations (reservoirs, thermal sources) the available data did not suffice to isolate the actual cause. [Pg.82]

Liquefied gas Water temperature range where RPTs were recorded (K) Temperature/ critical temperature of liquefied gas... [Pg.129]

Lemmon (1980) summarized a study carried out at Battelle-Columbus in which molten aluminum was dropped into water in a manner very similar to that used in the Alcoa program. The aluminum crucible had an 8-cm-diameter tap hole, and the water vessel was square, 30 cm on a side, and 25 cm deep. It was constructed of mild steel with one or more Plexiglas sides to allow observation. 5- to 20-kg drops of aluminum (1000-1330 K) were made. The height between the tap hole and vessel bottom varied from 48 to 53 cm. The water depth was 15 cm, and the water temperature ranged from 286 to 297 K. Fifty-four tests were run and, in many, highspeed photography was used to record any events. [Pg.169]

In general, foams will be more stable when they are generated with water at ambient or lower temperature. Preferred water temperatures range from 35 to 80°F (2 to 27°C). Either fresh or seawater may be used. Water containing known foam contaminants, such as detergents, oil residues, or certain corrosion inhibitors, may adversely affect foam quality and appropriate steps should be taken to ensure an adequate supply of suitable quality water. See NFPA 11 for more information on application rates. [Pg.213]

The water temperature will also influence the electrocoagulation process. A1 anode dissolution was investigated in the water temperature range from 2 to 90°C. The A1 current efficiency increase rapidly when the water temperature increase from 2 to 30°C. The temperature increase will speed up the destructive reaction of oxide membrane and increase the current efficiency. However, when the temperature was over 60°C, the current efficiency began to decrease. In this case, the volume of colloid Al(OH)3 will decrease and pores produced on the A1 anode will be closed. The above factors will be responsible for the decreased current efficiency. [Pg.254]

The Centers of Disease Control and Prevention (commonly referred to as the CDC) has recommended the ophmal level for fluoride in drinking water (2), which is dependent on water temperature and population type. As water temperature increases, the optimal level decreases. For community water systems (serving both adult and children) with water temperatures ranging from 50 to 53.7°F, the optimal level is 1.2 mg/L for community water systems with water temperature ranging from 79.3 to 90.5°F, the optimal level is 0.7 mg/L. Table 3 presents the optimal fluoride level for community water systems. As shown in Table 4, the optimal levels are significant higher for a school public water supply system. The optimal level for school children is 4.5 times the levels for the general population serviced by a community system. [Pg.297]

Nevertheless, it is now understood that HLB essentially depends on the surfactant, while the phase behavior and emulsion properties are also related to the water and oil phase nature, as well as to the temperature (100). The temperature was the preferred variable in the case of nonionic surfactants which are very sensitive to it, and an experimentally based concept was first introduced by Shinoda to quantify the formulation, i.e., the phase inversion temperature (PIT) (105, 106). It is known that the hydrophilicity of a nonionic surfactant decreses when temperature decreases. In water solution there exists a temperature at which the surfactant is no longer soluble and thus produces a separate phase. This so-called cloud point occurrence is related to the Shinoda PIT, which is essentially the same phenomenon, but in the presence of an oil phase whose nature could facilitate this separation and make it happen at a lower temperature. Although the PIT is limited to the liquid water temperature range of nonionic surfactants, its introduction was an important milestone because it was related not only to the surfactant, but also to the whole physicochemical environment (107), a feature that was shown to be essential by Winsor. [Pg.466]

The problem conditions are patterned after the FITS "D medium scale pouring mode experiments.7 in these experiments, roughly 20 kg of molten iron-alumina generated by a thermite reaction was dropped into water 15-66 cm deep contained in a square Plexiglas tank. The velocity of the melt on entry into the water was 5.7-7.3 m/s. Water temperature ranged from 284 K to 368 K, and pressure varied from 0.085 MPa to 1.1 MPa. [Pg.372]

Total dissolved soUds conductivity pH sUica (Si02), both total and reactive water temperature range... [Pg.79]

Hydrophobed silica mixed with hydrocarbons or silicone oil (mainly polydimethyl siloxane) is probably the most often used antifoam today. Hydrocarbons are solid or liquid, of petrochemical, synthetic, or natural origin. The material must melt and disperse in the washing liquor so that its melting point falls within a convenient water temperature range [72]. Silicone-based antifoams are not dependent on water hardness they are effective at dosages as low as 0.1%. They are compatible and effective in the presence of a wide variety of surfactants and for a broad spectrum of application conditions. [Pg.429]

Ahmad and colleagues studied SMEs made from palm stearin and palm fatty-acid distillates [8]. They conducted Terg-O-Tometer studies of built laundry powders, with and without phosphate. Evaluations took place in water hardness conditions ranging from 50 ppm to 500 ppm as CaCOj and from water temperatures ranging from room temperature to 60°C. They concluded that there was no difference in performance between the SME made from palm stearin and palm fatty-acid distillate. The SMEs were equal to or better than LAS in the nonphosphate test formulation at all conditions. The SMEs were equal to or better than LAS in both test formulations, with or without phosphate, in soft water. [Pg.131]

The metal looks like iron it exists in four allotropic modifications, stable over various temperature ranges. Although not easily attacked by air. it is slowly attacked by water and dissolves readily in dilute acids to give manganese(II) salts. The stable form of the metal at ordinary temperatures is hard and brittle—hence man ganese is only of value in alloys, for example in steels (ferroalloys) and with aluminium, copper and nickel. [Pg.384]

The relationship between the BET monolayer capacity of physically adsorbed water and the hydroxyl content of the surface of silica has been examined by Naono and his co-workers in a systematic study, following the earlier work by Morimoto. Samples of the starting material—a silica gel—were heated for 4 hours in vacuum at a succession of temperatures ranging from 25 to 1000°C, and the surface concentration of hydroxyl groups of each sample was obtained from the further loss on ignition at 1100°C combined with the BET-nitrogen area. Two complete water isotherms were determined at 20°C on each sample, and to ensure complete... [Pg.272]

Electrical Properties. Polytetrafluoroethylene is an excellent electrical insulator because of its mechanical strength and chemical and thermal stabihty as well as excellent electrical properties (Table 6). It does not absorb water and volume resistivity remains unchanged even after prolonged soaking. The dielectric constant remains constant at 2.1 for a temperature range of —40 to 250°C and a frequency range of 5 Hz to 10 GHz. [Pg.352]

Electrica.1 Properties. Because of excellent electrical properties, FEP is a valuable and versatile electrical insulator. Within the recommended service temperature range, PTFE and EEP have identical properties as electrical insulators. Volume resistivity, which is >10 H/cm, remains unchanged even after prolonged soaking in water surface resistivity is >10 H/sq. [Pg.361]

Formamide decomposes thermally either to ammonia and carbon monoxide or to hydrocyanic acid and water. Temperatures around 100°C are critical for formamide, in order to maintain the quaUty requited. The lowest temperature range at which appreciable decomposition occurs is 180—190°C. Boiling formamide decomposes at atmospheric pressure at a rate of about 0.5%/min. In the absence of catalysts the reaction forming NH and CO predominates, whereas hydrocyanic acid formation is favored in the presence of suitable catalysts, eg, aluminum oxides, with yields in excess of 90% at temperatures between 400 and 600°C. [Pg.508]

Ucon HTF-500. Union Carbide Corp. manufactures Ucon HTE-500, a polyalkylene glycol suitable for Hquid-phase heat transfer. The fluid exhibits good thermal stabHity in the recommended temperature range and is inhibited against oxidation. The products of decomposition are soluble and viscosity increases as decomposition proceeds. The vapor pressure of the fluid is negligible and it is not feasible to recover the used fluid by distiHation. Also, because the degradation products are soluble in the fluid, it is not possible to remove them by filtration any spent fluid usuaHy must be burned as fuel or discarded. The fluid is soluble in water. [Pg.504]

There are significant problems for one-step thermal water spHtting. In future nuclear and solar facihties, about 927°C is considered the upper temperature range, which is not sufficient for this reaction. Even if high temperature heat sources were available, materials of constmction would present difficulties. There would also be separation problems (155). [Pg.424]

Hydrogen Chloride—Water System. Hydrogen chloride is highly soluble in water and this aqueous solution does not obey Henry s law at ah concentrations. Solubhity data are summarized in Table 5. The relationship between the pressure and vapor composition of unsaturated aqueous hydrochloric acid solutions is given in Reference 12. The vapor—Hquid equiHbria for the water—hydrogen chloride system at pressures up to 1632 kPa and at temperatures ranging from —10 to +70° C are documented in Reference 13. [Pg.439]

This reaction is commonly known as the CO or water gas shift reaction. The conversion of CO by this reaction is slightly exothermic and favored by lower temperatures. The lower practical operating temperature range for this reaction is between 180 and 200°C (8). [Pg.454]

Ammonium lactate [34302-65-3] ia coaceatrated aqueous solutioas has beea coaverted to ammonia and the ester by alcoholysis at temperatures ranging from 100—200°C usiag a variety of alcohols and water entrainers, such as toluene. Ester yields ranging from 50—80% were obtained. This method has also been suggested as a recovery and purification method from impure solutions of lactate (29). However, a considerable amount of the lactate is not converted to the recoverable ester and is lost as lactamide (6). [Pg.512]


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See also in sourсe #XX -- [ Pg.468 ]




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