Design and testing of an emulsion liquid membrane pilot plant

Citation
Grm. Breembroek et al., Design and testing of an emulsion liquid membrane pilot plant, SEP SCI TEC, 35(10), 2000, pp. 1539-1571
Citations number
39
Categorie Soggetti
Chemistry
Journal title
SEPARATION SCIENCE AND TECHNOLOGY
ISSN journal
01496395 → ACNP
Volume
35
Issue
10
Year of publication
2000
Pages
1539 - 1571
Database
ISI
SICI code
0149-6395(2000)35:10<1539:DATOAE>2.0.ZU;2-X
Abstract
An emulsion liquid membrane (ELM) extraction rotating disc contactor (RDC) column with auxiliary equipment has been designed and tested. An ELM spray column was designed as well. ELM is a suitable technique for the removal of heavy metal ions from waste or process streams. However, no design rules a re available yet. This paper proposes and verifies a design procedure based on solvent extraction methods. The equipment was designed to reduce the 10 0 ppm cadmium concentration in a 90 Lk feed stream to 5% of its initial val ue, and to achieve a concentration factor of at least 12.5 in the strip pha se. Trilaurylamine (1%) in kerosene was used as the extractant solution. Th e RDC column diameter was 70 mm and its designed height was 2.2 m. The spra y column had a diameter of 50 mm and a designed height of 4.2 m. Both colum ns were constructed from five separate parts of 1 m height each to obtain t he necessary flexibility. Experiments showed a reduction of the cadmium con tent down to 1% of the initial value and a concentration factor of 14 with the RDC. The efficiency of the spray column experiment was 50%. The rotor s peed and the hold up in the RDC had to be kept lower (0.75 and 0.55 times, respectively) than the design values to avoid entrainment of the smallest d rops with the feed phase. The validity of the models used in the design was assessed by inserting the actual experimental conditions in the design equ ations. This resulted in a good coincidence of the actual and calculated ch aracteristic drop velocity, a good coincidence of most mass transfer coeffi cients, and a reasonable estimation of the number of equilibrium stages. Th e auxiliary equipment, comprising among others an electrostatic emulsion sp litter, operated as designed at optimal conditions. The splitter proved to be critical at smaller emulsion droplet sizes. It can be concluded that des ign methods for a solvent extraction column are suitable for ELM.