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Non conversion

Any non-conversed reactant of the suspension and the reaction product are deposited on fluidized-bed material after the drying process, and can be removed from the bed material by attrition. The dust due to the attrition is elutriated with the gas flow from the fluidized bed. [Pg.462]

Almost all chemical information systems work with tlicir own special type of connection table. They often use various formats distinguishing between internal and external connection tables. In most cases, the internal connection tables arc redundant, thus allowing maximum flexibility and increasing the speed of data processing. The external connection tables are usually non-redundant in order to save disk space. Although a connection table can be cprcsented in many different ways, the core remains the same the list of atoms and the list of bonds. Thus, the conversion of one connection table format into another is usually a fairly straightforward task. [Pg.42]

The scientific area is often characterized by a highly fluctuating and international workforce. This makes it necessary to document the source code and to represent e. g. the class structure in order to introduce new staff to the system easily. Conversely, non-existent documentation may lead to the necessity of reimplementation. [Pg.627]

Sharpless epoxidations can also be used to separate enantiomers of chiral allylic alcohols by kinetic resolution (V.S. Martin, 1981 K.B. Sharpless, 1983 B). In this procedure the epoxidation of the allylic alcohol is stopped at 50% conversion, and the desired alcohol is either enriched in the epoxide fraction or in the non-reacted allylic alcohol fraction. Examples are given in section 4.8.3. [Pg.126]

To obtain a reliable value of from the isotherm it is necessary that the monolayer shall be virtually complete before the build-up of higher layers commences this requirement is met if the BET parameter c is not too low, and will be reflected in a sharp knee of the isotherm and a well defined Point B. For conversion of into A, the ideal adsorptive would be one which is composed of spherically symmetrical molecules and always forms a non-localized film, and therefore gives the same value of on all adsorbents. Non-localization demands a low value of c as c increases the adsorbate molecules move more and more closely into registry with the lattice of the adsorbent, so that becomes increasingly dependent on the lattice dimensions of the adsorbent, and decreasingly dependent on the molecular size of the adsorbate. [Pg.103]

A representative list of conversion factors from non-SI to SI units is presented herewith. Factors are given to four significant figures. Exact relationships are followed by a dagger. A more complete Hst is given in the latest editions of ASTM E380 (4) and ANSI Z210.1 (6). [Pg.565]

W. A. Bulen, J. R. LeComte, R. C. Bums, and J. Hinkson, in A. San Pietro, ed., Non-Heme Iron Proteins Role in Lnerg Conversion Antioch Press, Yellow Springs, Ohio, 1965, p. 261. [Pg.95]

Pressure is defined as force per unit of area. The International System of Units (SI) pressure unit is the pascal (Pa), defined as 1.0 N /m. Conversion factors from non-SI units to pascal are given in Table 1 (see also Units and conversion factors front matter). An asterisk after the sixth decimal place indicates that the conversion factor is exact and all subsequent digits are 2ero. Relationships that are not followed by an asterisk are either the results of physical measurements or are only approximate. The factors are written as numbers greater than 1 and less than 10, with 6 or fewer decimal places (1). [Pg.19]

Thiirane 1,1-dioxides extrude sulfur dioxide readily (70S393) at temperatures usually in the range 50-100 °C, although some, such as c/s-2,3-diphenylthiirane 1,1-dioxide or 2-p-nitrophenylthiirane 1,1-dioxide, lose sulfur dioxide at room temperature. The extrusion is usually stereospeciflc (Scheme 10) and a concerted, non-linear chelotropic expulsion of sulfur dioxide or a singlet diradical mechanism in which loss of sulfur dioxide occurs faster than bond rotation may be involved. The latter mechanism is likely for episulfones with substituents which can stabilize the intermediate diradical. The Ramberg-Backlund reaction (B-77MI50600) in which a-halosulfones are converted to alkenes in the presence of base, involves formation of an episulfone from which sulfur dioxide is removed either thermally or by base (Scheme 11). A similar conversion of a,a -dihalosulfones to alkenes is effected by triphenylphosphine. Thermolysis of a-thiolactone (5) results in loss of carbon monoxide rather than sulfur (Scheme 12). [Pg.141]

The production of copper from sulphide minerals is accomplished with a preliminary partial roast of die sulphides before reaction widr air in the liquid state, known as mattes, to form copper metal (conversion). The principal sources of copper are minerals such as chalcopyrite, CuFeSa and bornite CuaFeSa, and hence the conversion process must accomplish the preferential oxidation of non, in the form of FeO, before the copper metal appears. As mentioned before, tire FeO-SiOa liquid system is practically Raoultian, and so it is relatively easy to calculate the amount of iron oxidation which can be canned out to form this liquid slag as a function of the FeO/SiOa ratio before copper oxidation occurs. The liquid slag has a maximum mole fraction of FeO at the matte blowing temperatures of about 0.3, at solid silica saturation. [Pg.339]

Industrially, chlorine is obtained as a by-product in the electrolytic conversion of salt to sodium hydroxide. Hazardous reactions have occuned between chlorine and a variety of chemicals including acetylene, alcohols, aluminium, ammonia, benzene, carbon disulphide, diethyl ether, diethyl zinc, fluorine, hydrocarbons, hydrogen, ferric chloride, metal hydrides, non-metals such as boron and phosphorus, rubber, and steel. [Pg.280]


See other pages where Non conversion is mentioned: [Pg.25]    [Pg.61]    [Pg.79]    [Pg.547]    [Pg.184]    [Pg.25]    [Pg.61]    [Pg.79]    [Pg.547]    [Pg.184]    [Pg.378]    [Pg.1143]    [Pg.2808]    [Pg.3070]    [Pg.102]    [Pg.200]    [Pg.886]    [Pg.18]    [Pg.327]    [Pg.286]    [Pg.361]    [Pg.367]    [Pg.114]    [Pg.342]    [Pg.311]    [Pg.224]    [Pg.419]    [Pg.114]    [Pg.89]    [Pg.146]    [Pg.26]    [Pg.34]    [Pg.36]    [Pg.40]    [Pg.83]    [Pg.113]    [Pg.341]    [Pg.55]    [Pg.228]    [Pg.21]    [Pg.347]    [Pg.71]    [Pg.134]    [Pg.182]   
See also in sourсe #XX -- [ Pg.255 , Pg.256 ]




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Conversion Factors for Non-SI Units

Conversion according to Non-Ideal CSTR with Dead Zone and Bypass

Conversion in Non-Ideal Flow Reactors

Conversion in Non-Thermal Plasma

Non-oxidative conversion

Sl/non-SI conversion factors

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