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Stabilizer leaching

In this chapter, we will present some contemporary results from our laboratory aimed toward blending the desirable properties of homogeneous and heterogeneous catalysts to create highly active, selective, and recoverable immobilized catalysts. The chapter covers organometaUic catalytic systems for polymerization reactions as well as small molecule reactions. Formation of single-site catalysts, recyclability, and stability/leaching issues will be addressed, as will studies on the effects of the immobilization procedure and the nature of the support structure on catalytic performance. Finally, a brief discussion on projected future directions for immobilized catalysts is presented. [Pg.442]

Eor pesticides to leach to groundwater, it may be necessary for preferential flow through macropores to dominate the sorption processes that control pesticide leaching to groundwater. Several studies have demonstrated that large continuous macropores exist in soil and provide pathways for rapid movement of water solutes. Increased permeabiUty, percolation, and solute transport can result from increased porosity, especially in no-tiUage systems where pore stmcture is stiU intact at the soil surface (70). Plant roots are important in creation and stabilization of soil macropores (71). [Pg.223]

Often, the immobilized product has a structural strength sufficient to prevent fracturing over time. Solidification accomplishes the objective by changing a non-solid waste material into a solid, monolithic structure that ideally will not permit liquids to percolate into or leach materials out of the mass. Stabilization, on the other hand, binds the hazardous constituents into an insoluble matrix or changes the hazardous constituent to an insoluble form. Other objectives of solidiflcation/stabilization processes are to improve handling of the waste and pri uce a stable solid (no free liquid) for subsequent use as a construction material or for landfilling. [Pg.176]

Polyphosphoric acid supported on diatomaceous earth (p. 342) is a petrochemicals catalyst for the polymerization, alkylation, dehydrogenation, and low-temperature isomerization of hydrocarbons. Phosphoric acid is also used in the production of activated carbon (p. 274). In addition to its massive use in the fertilizer industry (p. 524) free phosphoric acid can be used as a stabilizer for clay soils small additions of H3PO4 under moist conditions gradually leach out A1 and Fe from the clay and these form polymeric phosphates which bind the clay particles together. An allied though more refined use is in the setting of dental cements. [Pg.520]

Hall, M. S., and Leach, F. R. (1988). Stability of firefly luciferase in Tricine buffer and in a commercial enzyme stabilizer. /. Biolumin. Chemilumin. 2 41-44. [Pg.398]

S. Helf, Use of Saline Leaches to Stabilize Nitrocellulose , PATR 2550 (1958) 9) E.M. Smolin... [Pg.401]

Copper proteins, 1,168 5,720 models, 2,85 nonblue, 5,723 type 111, 5,724 Copper salts cellulose dyes, 6,38 Copper(I) salts stabilization, 6,786 Copper(II) salts ammoniacal leaching, 6,787 oxidant... [Pg.116]

The ability of polyvalent cations leached from the glass to suppress the free-fluoride ion concentration in basalt ground water is difficult to assess. Fluoride definitely enhances leaching and is the primary cause of the high concentrations of dissolved plutonium in the basalt ground-water leachate. Once the plutonium is dissolved, however, it is not possible to determine what fraction is stabilized by fluoride as opposed to other species leached from the glass. [Pg.342]

Leak R.E. Leech R. (1988) Challenge tests and their predictive stability. In Microbial Quality Assurance in Pharmaceuticals, Cosmetics and Toiletries (eds S.F. Bloomfield, R. Baird, R.E. Leak R. Leach), pp. 129-146. Chichester Ellis Horwood. [Pg.255]

The catalyst reuse is carried out without treating Pd/ ACF between the runs. Negligible leaching (<10% within the experimental error) was observed after catalyst reuse. Figure 8 shows the initial reaction rate and the selectivity for several runs. After activity drops in the first run, it stabilizes at 0.085 0.008 kmolHj/kgp /s, while selectivity to 1-hexene is 94+1%. Kinetic curves are identical from the second to the sixth runs. [Pg.297]

EQCM Analyses It was suggested by XPS analysis that the nonprecious metals were leached out from the alloy surface during CVs in acidic electrolyte solution. Therefore, we used an EQCM to measure the mass change at the electrode. The resolution and stability of our 10 MHz EQCM was +0.1 Hz, i.e., +0.44ngcm without any signal averaging. [Pg.320]


See other pages where Stabilizer leaching is mentioned: [Pg.1392]    [Pg.133]    [Pg.212]    [Pg.49]    [Pg.1392]    [Pg.133]    [Pg.212]    [Pg.49]    [Pg.2785]    [Pg.37]    [Pg.425]    [Pg.509]    [Pg.124]    [Pg.165]    [Pg.152]    [Pg.86]    [Pg.177]    [Pg.180]    [Pg.71]    [Pg.331]    [Pg.401]    [Pg.401]    [Pg.401]    [Pg.100]    [Pg.242]    [Pg.342]    [Pg.342]    [Pg.475]    [Pg.4]    [Pg.478]    [Pg.155]    [Pg.232]    [Pg.43]    [Pg.90]    [Pg.159]    [Pg.359]    [Pg.507]    [Pg.22]    [Pg.52]    [Pg.534]    [Pg.297]    [Pg.228]    [Pg.300]    [Pg.44]   
See also in sourсe #XX -- [ Pg.30 ]

See also in sourсe #XX -- [ Pg.72 , Pg.73 , Pg.146 ]




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