1997
DOI: 10.1080/01496399708000785
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An Improved Oil Emulsion Synthesis Method for Large, Porous Zirconia Particles for Packed- or Fluidized-Bed Protein Chromatography

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Cited by 8 publications
(4 citation statements)
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“…One series of papers [135,147,[155][156][157][158][159][160][161][162][163] affords a comparison of the type of pore structure, sintering behavior, diffusion behavior, and chromatographic performance of mesoporous zirconia made of the same colloid through two different methods to make spherical aggregates-that using an oil emulsion (cf. [13]) versus that using polymerization method (cf.…”
Section: Effect Of Synthesis Methods On the Pore Structurementioning
confidence: 99%
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“…One series of papers [135,147,[155][156][157][158][159][160][161][162][163] affords a comparison of the type of pore structure, sintering behavior, diffusion behavior, and chromatographic performance of mesoporous zirconia made of the same colloid through two different methods to make spherical aggregates-that using an oil emulsion (cf. [13]) versus that using polymerization method (cf.…”
Section: Effect Of Synthesis Methods On the Pore Structurementioning
confidence: 99%
“…This produces ca. 10 m spheres with pores ranging from 100 to 300 Å. Carr and co-workers [147] used a similar procedure, with a commercially available colloid and modified by rheological control of the aqueous phase and by the introduction of a reactive binder to enhance the stability and monodispersity of the resulting microspheres (however, they tended to make spheres on the order of 50 m in diameter). Shalliker et al [148][149][150][151][152][153][154] used a similar procedure, enhancing the rate and perhaps stability of the gel structure with the addition of urea.…”
Section: Zirconiamentioning
confidence: 96%
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“…The FBOM-zirconia particles were synthesized by the method of Robichaud et al (1997) and were screened with US standard sieves to select particles in the size range 75-103 m. The particles were washed with acid and base and elutriated prior to use as described elsewhere (Griffith et al, 1997). The bed was expanded using ddH 2 O with flow rates up to 75 mL/min.…”
Section: Expanded Bed Rtd and Protein Adsorptionmentioning
confidence: 99%