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Physical diying

Physical, Sulfamic acid is a diy acid having oithorhombic crystals. The pure crystals ate nonvolatile, nonhygroscopic, colodess, and ododess. The acid is highly stable up to its melting point and may be kept for years without change in properties. Selected physical properties of sulfamic acid are hsted in Table 1. Other properties are available in the hterature (5—8). [Pg.60]

Diying equipment may be classified in several ways. The two most useful classifications are based on (1) the method of transferring heat to the wet solids or (2) the handling characteristics and physical properties of the wet material. The first method of classification revels differences in diyer design and operation, while the second method is... [Pg.1184]

Initial. selection of diyers. Select those diyers which appear best suited to handhngthe wet material and the diy product, which fit into the continuity of the process as a whole, and which will produce a product of the desired physical properties. This preliminaiy selection can be made with the aid of Table 12-9, which classifies the various types of dryers on the basis of the materials handled. [Pg.1186]

These tests should establish the optimum operating conditions, the ability of the dryer to handle the material physically, product quality and characteristics, and diyer size. The principal manufacturers of diying equipment are usually prepared to perform the required tests on dryers simulating their equipment. Occasionally, simple laboratoiy experiments can serve to reduce further the number of diyers under consideration. [Pg.1186]

The above drying curves have been generated via testing on a plate-diyer simulator. The test unit duphcates the physical setup of the production diyer, therefore linear scale-up from the test data can be made to the full-scale diyer. Because of the thin product layer on each plate, diying in the unit closely follows the norm diying cui ve... [Pg.1217]

Various techniques are available to separate the different types of particles that may be present in a sohd mixture. The choice depends on the physicochemical nature of the sohds and on site-specific considerations (for example, wet versus diy methods). A key consideration is the extent of the liberation of the individual particles to be separated. Particles attached to each other obviously cannot be separated by direct mechanical means except after the attachment has been broken. In ore processing, the mineral values are generally liberated by size reduction (see Sec. 20). Rarely is liberation complete at any one size, and a physical-separation flow sheet wih incorporate a sequence of operations that often are designed first to rejec t as much... [Pg.1755]

The sulfur content of U.S. coals varies widely, ranging from a low of 0.2 percent to as much as 7 percent by weight, on a diy Basis. The estimated remaining U.S. coal reserves of all ranks, by sulfur content, are shown in Fig. 27-1. Extensive data on sulfur and sulfur reduc tion potential, including washability, in U.S. coals are given in Sulfur and Ash Reduction Potential and Selected Chemical and Physical Properties of United States Coal (U.S. Dept, of Energy, DOE/PETC, TR-90/7, 1990 TR-91/1 andTR-91/2, 1991). [Pg.2359]

Salts are obtained by direct neutralization of the acid with appropriate oxides, hydroxides, or carbonates. Sulfamic acid is a diy, non-volatile, non-hygroscopic, colourless, white, crystalline solid of considerable stability. It melts at 205°, begins to decompose at 210°, and at 260° rapidly gives a mixture of SO2, SO3, N2, H2O, etc. It is a strong acid (dissociation constant 1.01 x 10 at 25° solubility 25gper 100g H2O) and, because of its physical form and stability, is a convenient standard for acidimetry. Over 50000 tonnes are manufactured annually and its principal applications are in formulations for metal cleaners, scale removers, detergents and stabilizers for chlorine in aqueous solution. [Pg.742]

Table A-3. Some recommended simple physical and chemical diying methods for thirty-three common organic solvents -H- method gives superdry solvents with less than 1 ppm water -I- solvent sufficiently dry for most chemical applications (-I-) often used but less efficient — explosive hazard ( ) or other chemical reaction no entry means not recommended or no information in the literature. For extensive compilations of more sophisticated... [Pg.480]

The distribution of salinity in surface waters of the ocean is presented in Fig. 1.1. Because the concentrations for many major seawater constituents are unaffected by chemical reaction on the time scale of ocean circulation, local salinity distributions are controlled by a balance between two physical processes, evaporation and precipitation. This balance is reflected by low salinities in equatorial regions that result from extensive rain due to rising atmospheric circulation (atmospheric lows) and high salinities in hot diy subtropical g5Tes that flank the equator to the north and south (20-35 degrees of latitude) where the atmospheric circulation cells descend (atmospheric highs). [Pg.7]

Example 1—Dry 100 lbs. ofwetcake with an/ /fto/ volatiles content ofl5%(wetbasis) dovmXodiflnalvolatilescontent of less than 1 %. This will be achieved in a batch operation for lot identification, GMP and high quality standards. The loose bulk density of the wet cake is 45 lbs../ft. and the loose bulk density of the diy powder is 12 Ibs./ft. The temperature limit of the product is 145°F and the feed material is wet with ethanol. The product is a pharmaceutical which will be a finished product. The solvent is to be recovered for reuse, and its physical properties can be found in a handbook of hydrocarbons. The product is freeflowing in the dry state, but very tacky and pasty in the wet state. [Pg.747]

Physical e.xamination showed blood pressure 170/100 mm Hg and pulse 144/min. He was comatose. The skin was flushed, diy, and hot to the touch. The pupils were widely dilated and equal, with a minimal response to light. Rectal temperature was 39.8 °C. [Pg.75]

Removal of water from gases may be by physical or chemical means, and is commonly by adsorption on to a drying agent in a low-temperature trap. The effectiveness of diying agents depends on the vapour pressure of the hydrated compoimd - the lower the vapour pressure the less the remaining moisture in the gas. [Pg.30]

As already mentioned foe mass transfer coefficients used for calculations in chemical engineeting are rather parameters in foe calculation model than physical values. That is diy speaking of methods for determination of these coefficients we should distinguish methods for determination of foe mass transfer coefficients for foe piston flow model and for foe diffusion model. Since for foe latter model foese coefficients are connected with foe axial mixing coefficients in gas and liquid phase, foe methods for their determination are discussed after foe mefoods for determination of foe axial mixing coefficients. [Pg.123]


See other pages where Physical diying is mentioned: [Pg.1186]    [Pg.1190]    [Pg.1195]    [Pg.1726]    [Pg.1774]    [Pg.1959]    [Pg.369]    [Pg.267]    [Pg.173]    [Pg.483]    [Pg.139]    [Pg.350]    [Pg.179]    [Pg.115]    [Pg.10]    [Pg.716]    [Pg.79]    [Pg.411]    [Pg.716]    [Pg.452]    [Pg.41]    [Pg.177]    [Pg.26]    [Pg.1447]    [Pg.86]    [Pg.141]    [Pg.209]    [Pg.519]    [Pg.147]    [Pg.153]    [Pg.8]    [Pg.174]    [Pg.63]    [Pg.37]    [Pg.325]    [Pg.358]    [Pg.301]   
See also in sourсe #XX -- [ Pg.215 , Pg.239 , Pg.240 ]




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