Recovery of clay by microfiltration

Citation
T. Bilstad et L. Yastebo, Recovery of clay by microfiltration, DESALINATN, 127(2), 2000, pp. 177-180
Citations number
14
Categorie Soggetti
Chemical Engineering
Journal title
DESALINATION
ISSN journal
00119164 → ACNP
Volume
127
Issue
2
Year of publication
2000
Pages
177 - 180
Database
ISI
SICI code
0011-9164(20000201)127:2<177:ROCBM>2.0.ZU;2-9
Abstract
Pretreatment of dilute suspensions leads to separation of water and solids. Reuse of both water and flushed solids can be smart both economically and environmentally. Many industries produce effluents with mixtures of water a nd solid particles. Traditionally, the effluent is discharged via a sewer t o a receiving watercourse. Separation by microfiltration (MF) is a well sui ted method for recovery of production materials in dilute suspensions. Micr omembranes typically have pore sizes of 0.2 mu m. Larger particles are ther efore retained and the permeate is free of suspended solids. Bacteria, for example, are larger than 0.2 mu m. Removal of bacteria by MF therefore, may be defined as a physical "disinfection" process. The china producer Figgjo AS is big its Norway. The company produces cups and plates for restaurants , cruise-vessels and individual homes. The production of china results in e ffluents rich in clay and glaze particles. Traditionally, clay is difficult to separate without space-consuming and chemical-intensive processes such as coagulation, flocculation and sedimentation. After installing clay separ ation by MF, Figgjo AS has nearly eliminated clay in the effluent. The memb rane plant efficiently concentrates and recovers clay for reuse in the prod uction of china. The factory recovers 35 tons of clay annually by :MF. The savings in clay equates to a payback of the investment in MF equipment in 5 years. Compared to chemical coagulation for clay separation, the payback t ime is less than a year for a MF plant. There is no reuse of clay after che mical precipitation, and there is a sludge handling cost; transportation an d sludge deposit. The operation of the MF plant is automatic. The permeate flux is around 50 l/m(2)/h (lmh) at a cross-flow velocity of 2 m/s and an o perational pressure of maximum 2 kg/cm(2). The plant is flushed once a day with clean water. No chemical cleaning of the membranes is necessary.