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G Vapor Phase

The different chemical natures of the exposed and unexposed areas can be used for polymer pattern fabrication using a silylation technique, e.g., vapor phase hexamethyldisilazane (HMDS) treatment of the polymer films (32). HMDS is well-known to react with acidic hydroxyl groups to yield sUylated products. Here, HMDS reacts with phenolic hydroxyl groups, carboxylic groups, and peroxide groups, as shown below ... [Pg.459]

There are two general approaches for computer-aided identification of infrared spectra of unknown compounds [173,196-199,248-250]. The most common approach uses software designed to identify an unknown spectrum by its similarity to a limited number of reference spectra selected from a general or customized library of reference spectra measured under similar conditions (e.g. vapor phase, solid phase, etc.) Commercial... [Pg.778]

Subscripts xp = two phase g = vapor phase I — liquid phase p = pipe... [Pg.315]

Nicosia S, Galli G Vapor-phase methods for quantitative evaluation of prostaglandins and related compounds in biological samples. In Rrostaglandins and Thromboxanes Berti F, Samuelsson B, Velo GP (eds), New York and London, 1977, p 53-63. [Pg.70]

Enthalpies are referred to the ideal vapor. The enthalpy of the real vapor is found from zero-pressure heat capacities and from the virial equation of state for non-associated species or, for vapors containing highly dimerized vapors (e.g. organic acids), from the chemical theory of vapor imperfections, as discussed in Chapter 3. For pure components, liquid-phase enthalpies (relative to the ideal vapor) are found from differentiation of the zero-pressure standard-state fugacities these, in turn, are determined from vapor-pressure data, from vapor-phase corrections and liquid-phase densities. If good experimental data are used to determine the standard-state fugacity, the derivative gives enthalpies of liquids to nearly the same precision as that obtained with calorimetric data, and provides reliable heats of vaporization. [Pg.82]

Stringfellow G B 1989 Organometallic Vapor-Phase Epitaxy (San Diego, CA Academic)... [Pg.954]

The above direct process does not produce a high yield of ions, but it does form many molecules in the vapor phase. The yield of ions can be greatly increased by applying a second ionization method (e.g., electarn ionization) to the vaporized molecules. Therefore, laser desorption is often used in conjunction with a second ionization step, such as electron ionization, chemical ionization, or even a second laser ionization pulse. [Pg.384]

Processes rendered obsolete by the propylene ammoxidation process (51) include the ethylene cyanohydrin process (52—54) practiced commercially by American Cyanamid and Union Carbide in the United States and by I. G. Farben in Germany. The process involved the production of ethylene cyanohydrin by the base-cataly2ed addition of HCN to ethylene oxide in the liquid phase at about 60°C. A typical base catalyst used in this step was diethylamine. This was followed by liquid-phase or vapor-phase dehydration of the cyanohydrin. The Hquid-phase dehydration was performed at about 200°C using alkah metal or alkaline earth metal salts of organic acids, primarily formates and magnesium carbonate. Vapor-phase dehydration was accomphshed over alumina at about 250°C. [Pg.183]

J. B. MacChesney, P. B. O Connor, P. V. DiMarceUo, J. R. Simpson, and P. D. La2ay, "Preparation of Low-Loss Optical Pibers Using Simultaneous Vapor-Phase Deposition and Pusion," in Proceedings of t/je Tent/j Internationa/ Congress on G/ass, Ffoto, Japan, Vol. 6 Ceramics Society, Japan, 1974, pp. 50—54. [Pg.260]

Metalorganic Vapor Phase Epitaxy 1992," ia the Proceedings of the Sixth International Conference on Metalorganic Papor Phase Epitayy, Cambridge, Mass., June 1992 8—11, G. B. StriugfeUow and. J. Coleman, eds.,/ CystalGrowth, 124(1—4) (Nov. 1992). [Pg.438]

G. B. StringfeUow, Organometa//ic Vapor-Phase Epitayy Theory andPractice Academic Press, Inc., New York, 1989. [Pg.385]

Vitreous sihca does not react significantly with water under ambient conditions. The solution process involves the formation of monosilicic acid, Si(OH)4. Solubihty is fairly constant at low pH but increases rapidly when the pH exceeds 9 (84—86). Above a pH of 10.7 sihca dissolves mainly as soluble sihcates. Solubihty also increases with higher temperatures and pressures. At 200—400°C and 1—30 MPa (<10 300 atm), for example, the solubihty, S, of Si02 in g/kg H2O can be expressed as foUows, where d ls the density of the vapor phase and T is the absolute temperature in Kelvin. [Pg.500]

Fig. 6. Qualitative piessuie—tempeiatuie diagiams depicting ctitical curves for the six types of phase behaviors for binary systems, where C or Cp corresponds to pure component critical point G, vapor 1, Hquid U, upper critical end point and U, lower critical end point. Dashed curves are critical lines or phase boundaries (5). (a) Class I, the Ar—Kr system (b) Class 11, the CO2—CgH g system (c) Class 111, where the dashed lines A, B, C, and D correspond to the H2—CO, CH —H2S, He—H2, and He—CH system, respectively (d) Class IV, the CH —C H system (e) Class V, the C2H -C2H OH... Fig. 6. Qualitative piessuie—tempeiatuie diagiams depicting ctitical curves for the six types of phase behaviors for binary systems, where C or Cp corresponds to pure component critical point G, vapor 1, Hquid U, upper critical end point and U, lower critical end point. Dashed curves are critical lines or phase boundaries (5). (a) Class I, the Ar—Kr system (b) Class 11, the CO2—CgH g system (c) Class 111, where the dashed lines A, B, C, and D correspond to the H2—CO, CH —H2S, He—H2, and He—CH system, respectively (d) Class IV, the CH —C H system (e) Class V, the C2H -C2H OH...
As for LLE, an expression for G capable of representing hquid—hquid-phase splitting is required as for VLE, a vapor-phase equation of state for computing ( ) is also needed. Moreover, VLLE calculations can in principle and sometimes in practice be carried out with an equation of state vahd for ah. coexisting phases. [Pg.500]

Complex ions of Th(IV) have been studied and include M2 ThClg] [21493-66-3] where M = Li—Cs, (CH2)4N, or (C2H ) N. Under more extreme conditions, eg, molten KCl or vapor phase, ThCL [51340-85-3] ThCh [51340-84-2] ThCl g [53565-25-6] and ThCh are known to be important. Additional information on thorium chlorides can be found in the Hterature (81). [Pg.41]

Bismuth Penta.fIuoride, Bismuth(V) fluoride consists of long white needles that have been shown to have the same stmcture as the body-centered, tetragonal a-polymorph of uranium hexafluoride. The density of the soHd is 5.4 g/mL at 25°C. The soHd consists of infinite chains of trans-bridged BiF polyhedra dimers and trimers are present in the vapor phase (22). Bismuth pentafluoride may be prepared by the fluorination of BiF or... [Pg.129]

Vapor phases ia the B2O3 system iaclude water vapor and B(OH)3(g) at temperatures below 160°C. Appreciable losses of boric acid occur when aqueous solutions are concentrated by boiling (43). At high (600—1000°C) temperatures, HB02(g) is the principal boron species formed by equiUbration of water vapor and molten B2O3 (44). At stiU higher temperatures a trimer (HB02)3(g) (2) is formed. [Pg.191]

Analysts should not rely on databases developed by others unless citations and regression resiilts are available. Many improper conclusions have been drawn when analysts have relied upon the databases supplied with commercial simulators. While they may be accurate in the temperature, pressure, or composition range upon which they were developed, there is no guarantee that they are accurate for the unit conditions in question. Pure component and mixture correlations should be developed for the conditions experienced in the plant. The set of database parameters must be internally consistent (e.g., mixture-phase equilibria parameters based on the pure-component vapor pressures that will be used in the analysis). This ensures a consistent set of database parameters. [Pg.2554]

Tibbetts, G.G., Gorkiewicz, D.W., and Alig, R.A. A new reactor for growing carbon fibers from liquid- and vapor-phase hydrocarbons, Carbon, 993, 31(5), 809 814. Tibbetts, G.G., Bernardo, C.A., Gorkiewicz, D.W. and Alig R.L. Role of sulfur in the production of carbon fibers in the vapor phase. Carbon, 1994, 32(4), 569 576. [Pg.165]

Tibbetts, G.G., Endo, M. and Beetz, Jr. C.P., Carbon fibers grown from the vapor phase A novel material, SAMPE, Sept., Oct., 1986, 22(5). [Pg.165]

By assuming a balhstic delivery of material (e.g., from the vapor phase or through directed evaporation) we obtain at least a qualitative picture for the various growth forms of a faceted crystal surface. We assume that the adsorbed material ( A ) behaves differently from the crystalline substrate ( S ). [Pg.884]

In the distillation residue (5.7-6.3 g.) remain other byproducts, presumably l,l-dimethallyl-2-propanone, 3-methallyl-2,4-pentanedione, and 3,3-dimethallyl-2,4-pentanedione (indicated by vapor phase chromatography). The checkers carried out v.p.c. analyses using an 8-ft. column of 5% silicone oil XE-60 on Diatoport S at 100° for analysis of the distillate and 175° for analysis of the residue. [Pg.88]

However, if the azepine is C-monosubstituted, e.g. 14, or unsymmetrically substituted, then two isomeric 2-azabicycloheptadienes, e. g. 15 and 16, may result corresponding to electrocyclic ring closure involving C2-C5 or C4-C7 of the azepine ring. In practice, the ratio of the two isomers formed (which may be separated by vapor phase chromatography) varies with the position of the substituent.236 In contrast, irradiation of methyl 2,5-di-tm-butyl-l//-azepine-l-carboxylatein methanol yields only methyl 3,5-di-tert-bulyl-2-azabicycIo[3.2.0]hepta-3,6-diene-2-carboxylate (81 %).70... [Pg.177]

Phosphorous Trioxide (Diphosphorus trioxide). P203, mw 109.95, transparent monocl crysts, mp 23.8°, bp 173.1° in nitrogen atm, d 2.135 g/cc. Exists as P406 when in vapor phase or in benz soln. Disproportio nates into red P and P204 when heated above 210°. Sol in benz and C disulfide. When placed in cold w, H3PC>3 is formed. Prepd by treating PCI 3 with tetramethyl ammonium sulfite in liq S02 > or from the elements (Ref 6). It is highly toxic (Ref 7)... [Pg.734]

Fig. 4. Vapor-phase solubility of naphthalene in ethylene. Data points from G. A. M. Diepen and F. E. C. Scheffer, J. Am. Chem. Soc. 70, 4085 (1948) vapor-phase fugacities from (---) Redlich-Kwong equation (-) Ideal gas law. Fig. 4. Vapor-phase solubility of naphthalene in ethylene. Data points from G. A. M. Diepen and F. E. C. Scheffer, J. Am. Chem. Soc. 70, 4085 (1948) vapor-phase fugacities from (---) Redlich-Kwong equation (-) Ideal gas law.
For comparison, Battles et al. (15) determined the partial heats of sublimation of Pu02(g) and Pu0(g) above PuOi.33 over the temperature range 1937 to 2342 K by means of mass spectrometric measurements with Iridium effusion cells. The absence of Iridium oxides or Iridium species In the vapor phase Indicated that Iridium was nonreducing toward plutonia. The partial heats of sublimation calculated from the slopes of the temperature dependency data yielded values of 127.1 1.2 and 138.8 1.6 kcal/mol for Pu0(g) and Pu02(g) ... [Pg.118]

J.N. Michaels, and C.G. Vayenas, Kinetics of Vapor-Phase Electrochemical Oxidative Dehydrogenation of Ethylbenzene,/. Catal. 85, 477-488 (1984). [Pg.108]

M. Stoukides, and C.G. Vayenas, Transient and steady-state vapor phase electrocatalytic ethylene epoxidation, ACS Symposium Series 178 ("Catalysis under transient conditions") A.T. Bell and L.L. Hegedus, Eds., pp. 181-202 (1982). [Pg.273]


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