| 000 | 00000nam 2200000za 4500 |
| 001 | 9.841567 |
| 003 | CaOODSP |
| 005 | 20221107152123 |
| 007 | cr ||||||||||| |
| 008 | 170814s1973 oncad ob f000 0 eng d |
| 040 | |aCaOODSP|beng |
| 041 | |aeng|bfre |
| 043 | |an-cn--- |
| 086 | 1 |aM34-20/158E-PDF|zM34-20/158 |
| 100 | 1 |aSlater, M. J. |
| 245 | 10|aContinuous ion exchange in fluidized beds |h[electronic resource] / |cM.J. Slater and P. Prudhomme, Extraction Metallurgy Division. |
| 260 | |aOttawa : |bInformation Canada, |c1973. |
| 300 | |aiv, 79 p. : |bcharts, ill. |
| 490 | 1 |aTechnical bulletin ; |vTB 158 |
| 500 | |aCover title. |
| 500 | |a"September 1972." |
| 500 | |aDigitized edition from print [produced by Natural Resources Canada]. |
| 504 | |aIncludes bibliographical references (p. 30-31). |
| 520 | |a“A continuous ion-exchange plant using a multi-stage fluidized-bed extraction column coupled with moving-bed regeneration and wash columns has been built and tested. Hydrodynamic studies on resins and ore leach pulps have been made and a mathematical model has been developed to predict the performance of the extraction column. Clarified solutions from the leaching of uranium ore and leach pulps of 5 and 10 w/o have been used with IRA 430 ion exchange resin. The mathematical model requires refinement but its actual performance has been satisfactory for predicting the extraction of uranium"--Summary, p. i. |
| 546 | |aIncludes summary in French. |
| 692 | 07|2gccst|aMinerals |
| 692 | 07|2gccst|aProcessing |
| 692 | 07|2gccst|aEquipment |
| 692 | 07|2gccst|aDesign |
| 700 | 1 |aPrudhomme, P. |
| 710 | 1 |aCanada. |bNatural Resources Canada. |
| 710 | 1 |aCanada. |bMines Branch. |
| 830 | #0|aTechnical bulletin (Canada. Dept. of Energy, Mines and Resources. Mines Branch)|vTB 158|w(CaOODSP)9.834857 |
| 856 | 40|qPDF|s1.62 MB|uhttps://publications.gc.ca/collections/collection_2017/rncan-nrcan/M34-20/M34-20-158-eng.pdf |
| 986 | |a300041 |