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Selection Requirements

When the materials handled are noncorrosive, the flame arrester vendor s standard materials of constrnction for the honsing and arrester element are commonly nsed. For noncorrosive service honsings are normally available in alnminnm, carbon steel, dnctile iron, and 316 stainless steel the elements are commonly available in alnminnm or 316 stainless steel. [Pg.116]

In some cases, it may be desirable to specify an all stainless steel arrester to avoid contamination of the stored liqnid by mst or other particles from the honsing. Note that certain metals may catalyze polymerization of vapors in gas streams containing monomers, which will then be deposited on the flame arrester elements and hasten blockage. Also note that mst may be transported to the flame arrester from npstream sonrces. [Pg.116]

Consideration shonld be given to the corrosion allowance for flame arrester elements and honsings. Element corrosion will rednce the effectiveness of the arrester to qnench a flame and withstand the destmctive pressnre effects of a detonation. Also, increased element thickness will allow for greater periods between element replacement. [Pg.117]

Corrosion resistance can also be provided by lining a carbon steel honsing with stainless steel or other alloy. [Pg.117]


Maximum selectivity requires a minimum ratio rjr in Eq. (2.17). A high conversion in the reactor tends to decrease Cfeed- Thus... [Pg.26]

Because lactic acid has both hydroxyl and carboxyl functional groups, it undergoes iatramolecular or self-esterificatioa and forms linear polyesters, lactoyUactic acid (4) and higher poly(lactic acid)s, or the cycUc dimer 3,6-dimethyl-/)-dioxane-2,5-dione [95-96-5] (dilactide) (5). Whereas the linear polyesters, lactoyUactic acid and poly(lactic acid)s, are produced under typical condensation conditions such as by removal of water ia the preseace of acidic catalysts, the formation of dilactide with high yield and selectivity requires the use of special catalysts which are primarily weakly basic. The use of tin and ziac oxides and organostaimates and -titanates has been reported (6,21,22). [Pg.512]

Selection. Suspended magnet selection requires deterrnination of the burden depth using one of the following formulas. For installation flat over the belt or transverse self-cleaned mounting, the burden design is calculated as... [Pg.421]

Packed towers are used in some distillation operations in preference to plate towers. Usually the selection requires an understanding of the fouling characteristics of fluids of the system. These towers have been used even in polymer forming operations. However, other contacting devices can be cleaned easier. For some processes the packed tower is much more effective as well as cheaper than a tray tower. [Pg.370]

The wide choice available in plastics makes it necessary to select not only between TPs, TSs, reinforced plastics (RPs), and elastomers, but also between individual materials within each family of plastic types (Chapters 6 and 7). This selection requires having data suitable for making comparisons which, apart from the availability of data, depends on defining and recognizing the relevant plastics behavior characteristics. There can be, for instance, isotropic (homogeneous) plastics and plastics that can have different directional properties that run from the isotropic to anisotropic. Here, as an example, certain... [Pg.137]

We have developed a quantitative structure-activity model for the variations in potency among the nitrosamines and, more recently, a related model for the variation in target organ for a smaller set of nitrosamines. We are currently developing a model for interspecies variation in susceptibility toward carcinogenic nitrosamines. The model for organ selectivity requires terms for the parent nitrosamine as well as for the hypothesized metabolites while the model for potency variations contains terms only for the unmetabolized parent compound. [Pg.77]

It has been long believed that a lithium ion-selective electrode would render obsolete the flame photometer in the clinical laboratory. Lithium is administered to manic depressive psychiatric patients. Since the therapeutic range (0.5-1.5 mM) is quite close to the toxic range (>2 mM), it must be closely monitored. Most of the iono-phores propo d to date have not met the Li" /Na selectivity required for an interference-free assay. However, it has been reported that calibration in the presence of 140 mMNa permitted the analysis of Li in serum The errors observed are due to fluctuations in the Na concentrations in the sample. More selective ionophores would certainly improve the accuracy of this method. [Pg.61]

Chakraborty, S., Sengupta, C., Roy, K. Exploring QSAR with E-state index Selectivity requirements for COX-2 versus COX-1 binding of terphenyl methyl sulfones and sulfonamides. Eioorg. Med. Chem. Lett. 2004, 14, 4665-4670. [Pg.107]

During the detailed analysis, each alternative is assessed against the evaluation criteria. The results provide decision-makers with sufficient information to adequately compare the alternatives, select an appropriate remedy for a site, and demonstrate satisfaction of the CERCLA remedy selection requirements in the record of decision ... [Pg.605]

Maximum selectivity requires a minimum ratio r2/ri in Equation 5.65. A batch or plug-flow reactor maintains higher average concentrations of feed (CFeed) than a mixed-flow reactor, in which the incoming feed is instantly diluted by the PRODUCT and BYPRODUCT. If ax > a2 in Equations 5.64 and 5.65 the primary reaction to PRODUCT is favored by a high concentration of FEED. If ax < a2 the primary reaction to PRODUCT is favored by a low concentration of FEED. Thus, if... [Pg.91]

Nierkens, S. et al., Selective requirement for CD40-CD154 in drug-induced type 1 versus type 2 responses to trinitrophenyl-ovalbumin. J. Immunol., 168, 3747, 2002. [Pg.483]

It can be seen that most of the substances prohibited in sport are screened for by hyphenated chromatographic mass spectrometric techniques. Confirmation is also done using such techniques. The reason for this is that mass spectrometry coupled with chromatography provides the sensitivity and selectivity required to detect and... [Pg.227]

Finally, the most complex synthetic reaction clearly catalysed by RNA molecules generated by in vitro selection is the formation of the C-N bond of a nucleoside (Scheme 7), from 4-thiouracil and most of the natural substrate for the natural (uracil phos-phoribotransferase) reaction.1461. (Thiouracil was used because it is easily tagged by alkylation on sulfur.) The catalytic RNAs produced by 11 rounds of selection required Mg++ cations and had kcat as high as 0.13 min-1,with kcaJKM at least 107 times greater than the (undetectable) uncatalyzed reaction. Once again these systems are convincing, rather efficient enzyme mimics. [Pg.348]

The multi-functionality of metal oxides1,13 is one of the key aspects which allow realizing selectively on metal oxide catalysts complex multi-step transformations, such as w-butane or n-pentane selective oxidation.14,15 This multi-functionality of metal oxides is also the key aspect to implement a new sustainable industrial chemical production.16 The challenge to realize complex multi-step reactions over solid catalysts and ideally achieve 100% selectivity requires an understanding of the surface micro-kinetic and the relationship with the multi-functionality of the catalytic surface.17 However, the control of the catalyst multi-functionality requires the ability also to control their nano-architecture, e.g. the spatial arrangement of the active sites around the first centre of chemisorption of the incoming molecule.1... [Pg.365]

Rigorous treatment of the para-selectivity requires a knowledge of the intrinsic value of the rate constant for all the reactions involved and of the absolute value of the crystal size and of the diffusivity, all under reaction conditions. These values are obtainable only with considerable difficulty and effort. As has been mentioned, the 30 percent sorption time for o-xylene at 120°c, t0.3/ is proportional to the actual values, r2/D. [Pg.296]

Few well characterized, validated methods are available for the determination of w-hexane in blood. A purge-and-trap method for volatiles has been developed and validated by researchers at the Centers for Disease Control and Prevention (CDC) (Ashley et al. 1992, 1994). Extension of the method to include /7-hexane should be possible. Current analytical methods utilize capillary GC columns and MS detection to provide the sensitivity and selectivity required for the analysis. Detection limits are in the low ppb range (Brugnone et al. 1991 Schuberth 1994). Headspace extraction followed by GC analysis has also been utilized for the determination of /7-hexanc in blood (Brugnone et al. 1991 Michael et al. 1980 Schuberth 1994) however, very little performance data are available. [Pg.209]

High sensitivity, essential for the detection of trace amounts of analytes, in combination with high selectivity, required for the examination of challenging matrices, is also necessary. [Pg.150]

S is the selectivity of photon absorption under the particular experimental conditions, and 8 is the relative abundance of the desired isotope. Equation 8.19 shows, for example, that S values on the order of 103 are required before more than about 10% of photons are used to excite D in natural abundance H/D mixtures (8 1.5 x 10-4). The selectivity required for uranium separation is less because > 8(D). [Pg.283]

In order to achieve selective oxide and nitride etching, additives to F-source plasmas are chosen to make a F-deficient chemical environment. These include H2, C2H4 and CH4 which are quite efficient F scavengers. The amount of additive necessary remains more an art than a science because oxide and nitride selectivity requires operation in an environment very close to the demarcation between etching and polymerization shown in Figure 10. In fact in some cases (57,59) polymer deposition on Si occurs... [Pg.240]

Most polymerisation reactions occur via a complex reaction scheme. Relatively few reactant species are involved (sometimes only one) and these are usually well-defined. However, the reaction products can be described in a number of ways. The polymer molecules produced in these reactions vary in size in some cases the size distribution can be very wide. In effect, a polymerisation reaction produces a large number of reaction products and reaction selectivity requires special treatment. For some purposes, the polymer molecules can be treated as a combined group which is referred to generally as polymer . However, the physical properties of any given type of polymer depend on its molecular weight distribution. Therefore, it is often necessary to obtain a quantitative description of the product size distribution. This will depend on both the kinetic scheme for the polymerisation reaction and the mixing conditions in the polymerisation reactor. [Pg.131]

For a given subset of chemicals, where cp CP, these constraints control the production of different processes based on the upper and lower demands of the petrochemical market for the final products. In constraint (4.3), defining the binary variables yp cm for each process m Mpet is required for the process selection requirement as y ( m will equal 1 only if process m is selected or zero otherwise. Furthermore, if only process m is selected, its production level must be at least equal to the process minimum economic capacity B for each m Mpet, where Ku is a valid upper bound.. This can be written for each process m as follows ... [Pg.83]

All these arguments require a single reactant A on which to base the calculation of selectivity. For more complex situations we can stiU determine how the selectivity varies with conversion in PFTR and CSTR, but calculation of the selectivity requires complete solution of the mass-balance equations. [Pg.175]


See other pages where Selection Requirements is mentioned: [Pg.526]    [Pg.898]    [Pg.116]    [Pg.118]    [Pg.146]    [Pg.730]    [Pg.27]    [Pg.89]    [Pg.241]    [Pg.246]    [Pg.13]    [Pg.184]    [Pg.375]    [Pg.620]    [Pg.627]    [Pg.639]    [Pg.260]    [Pg.302]    [Pg.365]    [Pg.165]    [Pg.295]    [Pg.56]    [Pg.344]    [Pg.1]    [Pg.258]    [Pg.30]   


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Acid Strength Requirements for Product Control and Influence of Spatial Distribution on Selectivity

Agitators, power requirements selection

Isotope selection requirements

Material selection establishing operational requirements

OSHA Respirator Requirements for Selected Chemicals

Para-selectivity requirements

Requirement for High Selectivity Slurry

Requirements for selection of components and subsystems

Selective pulse requirements

Selectivity of energy requirements

Separation, energy requirement selection

Test site requirements, evaluation and selection

Thermophysical Properties Required for Selective Solvents

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