741 - 760 |
Role of bubble size in flotation of coarse and fine particles - A review Tao D |
761 - 780 |
Application of molecular connectivity indices to the design of supercritical carbon dioxide-soluble metal ion extractants: SC-CO2 Solubilities of symmetrically substituted alkylenediphosphonic acids McAlister DR, Dietz ML, Stepinski D, Zalupski PR, Dzielawa JA, Barrans RE, Hess JN, Herlinger AW |
781 - 797 |
Effect of rheological properties on mass transfer of Cr(VI) through a supported liquid membrane with non-Newtonian liquid Park SW, Jung HI, Kim TY, Lee JW |
799 - 810 |
Transport kinetics of Hg2+ through bulk liquid membrane using calix[4]arene ketone derivative as carrier Alpoguz HK, Memon S, Ersoz M, Yilmaz M |
811 - 831 |
Removal of arsenic anions from water using polyelectrolyte-enhanced ultrafiltration Pookrod P, Haller KJ, Scamehorn JF |
833 - 854 |
The influence of membrane surface properties on fouling in a membrane bioreactor for wastewater treatment Kim DS, Kang JS, Lee YM |
855 - 877 |
Flowdynamic modeling of bale-type catalytic distillation packings Caetano MG, Gonzalez JC, Solari RB |
879 - 891 |
Precipitation of sulfur dioxide from gaseous feed by oxidative chemisorption Vorbach M, Marr R, Siebenhofer M |
893 - 909 |
Cu(II) recovery from aqueous systems by flotation Stoica L, Oproiu GC |
911 - 923 |
Removal of phenols from aqueous solutions by purolite A-510 resin Ku Y, Lee KC, Wang W |
925 - 940 |
Removal of heavy metal ions from solutions using zeolites. III. Influence of sodium ion concentration in the liquid phase on the kinetics of exchange processes between cadmium ions from solution and sodium ions from zeolite A Biskup B, Subotic B |
941 - 957 |
Synthesis, characterization, and metal extractive behavior of functionalized AXAD-16 polymeric matrix using oxyacetone acetamide Prabhakaran D, Subramanian MS |
959 - 974 |
Aspects of the adsorption behavior of Cu2+Zn2+, and Ni2+ ions on lithium titanate ion exchanger El-Naggar IM, Zakaria ES, Ali IM |