000080677 001__ 80677
000080677 005__ 20181203020250.0
000080677 0247_ $$2doi$$a10.1021/i200027a015
000080677 02470 $$2ISI$$aA1984TM51400015
000080677 037__ $$aARTICLE
000080677 245__ $$aInfluence of the physical properties of the liquid on axial dispersion in packed columns
000080677 260__ $$c1984
000080677 269__ $$a1984
000080677 336__ $$aJournal Articles
000080677 520__ $$aThe effects of the viscosity and surface tension on the axial dispersion and liq. holdup was investigated in a 0.3-m-diam. packed column with countercurrent gas-liq. flow. The axial dispersion appeared to be independent of the viscosity and surface tension. The traditional complex form of correlating Peclet nos. as a function of the interstitial Reynolds and Galileo nos. may be replaced by a much simpler form contg. only the Froude no. as a correlating variable for the liq. phase. The axial dispersion depended slightly on the gas flow rate. Differences in axial dispersion and holdup were obsd. as a function of the radial position. [on SciFinder (R)]
000080677 700__ $$0240951$$aVon Stockar, Urs$$g106679
000080677 700__ $$aCevey, Pierre F.
000080677 773__ $$j23$$k4$$q717-24$$tIndustrial & Engineering Chemistry Process Design and Development
000080677 909C0 $$0252160$$pLGCB$$xU10179
000080677 909CO $$ooai:infoscience.tind.io:80677$$particle
000080677 937__ $$aLGCB-ARTICLE-1984-001
000080677 970__ $$a65/LGCB
000080677 973__ $$aEPFL$$rREVIEWED$$sPUBLISHED
000080677 980__ $$aARTICLE