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Phosphorous acid, model

Refer to Table C-1 in Appendix C for a key to atom color conventions. Then, identify the two hydrogen atoms bonded to oxygen atoms in the sulfuric acid model and the three hydrogen atoms bonded to oxygen atoms in the phosphoric acid model. [Pg.601]

Rumpf B, Maurer G (1994) Solubility of ammonia in aqueous solutions of phosphoric acid model development and application. J Solution Chem 23 37-51... [Pg.423]

Because of this extreme sensitivity, attention shifted to an acidic system, the phosphoric acid fuel cell (PAFC), for other applications. Although it is tolerant to CO, the need for liquid water to be present to facilitate proton migration adds complexity to the system. It is now a relatively mature technology, having been developed extensively for stationary power usage, and 200 kW units (designed for co-generation) are currently for sale and have demonstrated 40,000 hours of operation. An 11 MW model has also been tested. [Pg.528]

Phosphoric acid ester was used as a model for the estimation of concentration of a reagent in an adsorbed layer by optical measurements of the intensity of a beam reflecting externally from the liquid-liquid interface. The refractive index of an adsorbed layer between water and organic solution phases was measured through an external reflection method with a polarized incident laser beam to estimate the concentration of a surfactant at the interface. Variation of the interfacial concentration with the bulk concentration estimated on phosphoric acid ester in heptane and water system from the optical method agreed with the results determined from the interfacial tension measurements... [Pg.614]

It is important to emphasize that often — but not always — the performance of a product with a chemical depends heavily on the manufacturer and a specific product model. A model that performs well with one chemical may perform poorly with another chemical, even when the chemicals are in the same chemical class. This is illustrated by the Edmont Model 37-165 glove which was tested against all five acids. This glove shows good protective properties with hydrochloric, perchloric, and phosphoric acids, but exhibits degradation in nitric and sulfuric acids. [Pg.64]

B. Solvolysis of Phosphoric Acid Derivatives.—Interest continues in neighbouring-group participation in the solvolysis of phosphate esters. As a potential model compound for investigating the mechanism of ribo-nuclease action, the phenyl hydrogen phosphate ester of c/j-3,4-tetrahydro-furandiol (24) has been the subject of a detailed study. Above (and probably also below) pH 4 hydrolysis gives solely the cyclic phosphate (25)... [Pg.100]

Figure 3. A model of a porous oxide film formed at 120 V in a phosphoric acid solution, according to Heber.10... Figure 3. A model of a porous oxide film formed at 120 V in a phosphoric acid solution, according to Heber.10...
Nucleic acids, DNA and RNA, are attractive biopolymers that can be used for biomedical applications [175,176], nanostructure fabrication [177,178], computing [179,180], and materials for electron-conduction [181,182]. Immobilization of DNA and RNA in well-defined nanostructures would be one of the most unique subjects in current nanotechnology. Unfortunately, a silica surface cannot usually adsorb duplex DNA in aqueous solution due to the electrostatic repulsion between the silica surface and polyanionic DNA. However, Fujiwara et al. recently found that duplex DNA in protonated phosphoric acid form can adsorb on mesoporous silicates, even in low-salt aqueous solution [183]. The DNA adsorption behavior depended much on the pore size of the mesoporous silica. Plausible models of DNA accommodation in mesopore silica channels are depicted in Figure 4.20. Inclusion of duplex DNA in mesoporous silicates with larger pores, around 3.8 nm diameter, would be accompanied by the formation of four water monolayers on the silica surface of the mesoporous inner channel (Figure 4.20A), where sufficient quantities of Si—OH groups remained after solvent extraction of the template (not by calcination). [Pg.134]

Fogli et al. developed and validated an HPLC method with fluorescence detection for simultaneous routine TDM of anthracyclines and their metabolites.27 They coupled a Waters LC Module I Plus system equipped with a WISP 416 autosampler with a Model 474 scanning fluorescence spectrophotometer. The stationary phase was a Supelcosil LC-CN column (250 x 4.6 mm, 5 /um particle size) with a /iBondapak-CN guard column. The mobile phase consisted of 50mM monobasic sodium phosphate buffer and acetonitrile (65 35 v/v), adjusted to pH 4.0 with phosphoric acid. The flow rate was 1 mL/min. The fluorescence detection was set at excitation wavelengths of 233, 254, and 480 nm and at an emission wavelength of 560 nm. [Pg.302]

Shah V.B. ASPEN Models for Solid Oxide Fuel Cell, Molten Carbonate Fuel Cell and Phosphoric Acid Fuel Cell Prepared by EG G Washington Analytical Services Center for the Morgantown Energy Technology Center under Contract No. DE-AC21-85MC21353, 1988. [Pg.282]

The beginning of modeling of polymer-electrolyte fuel cells can actually be traced back to phosphoric-acid fuel cells. These systems are very similar in terms of their porous-electrode nature, with only the electrolyte being different, namely, a liquid. Giner and Hunter and Cutlip and co-workers proposed the first such models. These models account for diffusion and reaction in the gas-diffusion electrodes. These processes were also examined later with porous-electrode theory. While the phosphoric-acid fuel-cell models became more refined, polymer-electrolyte-membrane fuel cells began getting much more attention, especially experimentally. [Pg.442]

The earliest models of fuel-cell catalyst layers are microscopic, single-pore models, because these models are amenable to analytic solutions. The original models were done for phosphoric-acid fuel cells. In these systems, the catalyst layer contains Teflon-coated pores for gas diffusion, with the rest of the electrode being flooded with the liquid electrolyte. The single-pore models, like all microscopic models, require a somewhat detailed microstructure of the layers. Hence, effective values for such parameters as diffusivity and conductivity are not used, since they involve averaging over the microstructure. [Pg.464]

The solids analysis described above can be taken to yet another level by correlating the color measurement to chemical properties. An excellent model system is vanadium pyrophosphate (VPO), which is a well-known catalyst for butane oxidation to maleic anhydride. During the synthesis of the catalyst precursor, solid V2O5 particles are dispersed in a mixture of benzyl alcohol and i-butanol. In this slurry phase, the vanadium is partly reduced. Addition of phosphoric acid leads to a further reduction and the formation of the VPO structure. With a diffuse reflectance (DR) UV-vis probe by Fiberguide Ind., the surface of the suspended solid particles could be monitored during this slurry reaction. Four points can be noted from Figure 4.4 ... [Pg.97]

Notably, the aminoalkylation reaction did not occur with iV-protected indoles revealing the crucial role of the free N-H group for the activation by the phosphoric acid. This prompted the authors to postulate the transition state model depicted in Fig. 6. [Pg.408]

A full discussion of these models will follow in Section 21.3. At this point we will deal only with a special version of Eq. 21-30 in which there is no back-reaction from B to A and no external input of chemical B. As an example imagine the case of the pollution of a pond by a pesticide A that in the water is transformed into another compound B that is more toxic than the original compound. For instance, thiophos-phoric acid ester is transformed to the corresponding phosphoric acid ester (see Chapters 2 and 13). Then it would be important to predict the maximum concentrations of A and B in the pond and to estimate the necessary time until the pollutant concentration has fallen below a certain threshold. Such a case will be discussed in Illustrative Example 21.4 below. [Pg.978]

The several attempts, published in the literature, to describe the kinetics of vapour phase olefin (mostly ethylene) hydration can be classified into two groups according to the basic model used. One model, for reactions catalysed by phosphoric acid supported on solids, treats the kinetics as if the process were homogeneous acid catalysis and takes into account the acid strength of the supported acid. Thus, a semiempirical equation for the initial reaction rate [288]... [Pg.324]

T0 prepare models of TA, the corresponding cyclic alkylene phosphoric acids cannot be directly polymerized because the presence of acidic protons of the phosphate group makes the ionic polymerization impossible. Thus, cyclic phosphorus compounds with blocked third functions have to be used. These are phosphates., phosphoramidates and phosphites. After polymerization the obtained polymer is converted by deblocking into the polyalkylene phosphate, e.g. polysalt or polyacid form. [Pg.150]

Free fatty acids are separable by GC by the inclusion of phosphoric acid in the packing so, for HPLC analysis, the phosphoric acid or other equivalent strong acid is included in the mobile phase. On a SUPELCOSIL LC 18 column, a model mixture of free fatty acids was separated with a mobile phase containing tetrahydrofuran, acetonitrile, water, and phosphoric acid (6 64 30 0.1) at pH 2 (Fig. 1) (15). Oleic and elaidic acids, palmitoleic and palmitelaidic acids, and linoleic and linoelaidic acids were well separated, but margarine fatty acids presented a difficult problem. Ultraviolet detection of 220 nm was used to prepare this chromatogram. [Pg.175]

Gas chromatography analysis was done on a Perkin-Elmer model 800 unit using dual X 6 columns packed with silanized Chromasorb W (product of Johns-Manville) coated with 5% neopentylglycolsebecate and y2% phosphoric acid. The column temperature was programmed from 100° to 240° C. at 8°/imm during analysis. [Pg.240]

Descriptors (Acyclic + Phosphoric acids + Tertiary amines) (Model 75)... [Pg.318]

For aliphatic chemicals with phosphoric acid or a tertiary amine, the Acyclic Aliphatic + ( 75) model should be used, which consists of the following equation ... [Pg.323]

Acyclic Aliphatic+ Model 75 for Phosphoric Acid and Tertiary Amine. [Pg.326]

The disintegration degree of a phosphorite flotation concentrate in the functions of temperature and impurity contents in phosphorous acid has been described by a second-order regression model ... [Pg.443]


See other pages where Phosphorous acid, model is mentioned: [Pg.21]    [Pg.64]    [Pg.122]    [Pg.361]    [Pg.138]    [Pg.249]    [Pg.332]    [Pg.445]    [Pg.464]    [Pg.482]    [Pg.298]    [Pg.24]    [Pg.10]    [Pg.303]    [Pg.131]    [Pg.134]    [Pg.288]    [Pg.325]    [Pg.329]    [Pg.944]    [Pg.131]    [Pg.101]    [Pg.329]    [Pg.55]    [Pg.335]    [Pg.407]   


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