Solids management and removal for intensive land-based aquaculture production systems

Citation
Sj. Cripps et A. Bergheim, Solids management and removal for intensive land-based aquaculture production systems, AQUACULT EN, 22(1-2), 2000, pp. 33-56
Citations number
109
Categorie Soggetti
Aquatic Sciences
Journal title
AQUACULTURAL ENGINEERING
ISSN journal
01448609 → ACNP
Volume
22
Issue
1-2
Year of publication
2000
Pages
33 - 56
Database
ISI
SICI code
0144-8609(200005)22:1-2<33:SMARFI>2.0.ZU;2-X
Abstract
This review aims to identify and examine realistic aquaculture waste solids management strategies. The main reason for treating solids to be discharge d from flow-through systems is to reduce potential negative impacts on the surrounding aquatic environment. In reuse and recycle systems, solids manag ement will be required to maintain culture water quality. In such cases, so lids management will often be designed to be combined with other unit proce sses. Solids concentrations in the untreated effluent from flow-though farm s are low at around 5-50 mg l(-1), and do not appear to have altered greatl y within the last 20 years. These solids can commonly carry 7-32% of the to tal nitrogen and 30-84% of the total phosphorus in the wastewater. Feed qua lity and feeding management can be manipulated to reduce the quantity of wa ste solids produced. Decreases in the specific water consumption within a f arm, increase the concentration of solids in the effluent, which results in an increase in particle separation efficiency. Particles should be separat ed from the culture stock and the primary effluent flow quickly and efficie ntly (i.e. at high solids concentrations). This can be achieved by within-t ank separation systems, often comprising a separate low-flow particle outle t. Rotating microscreens are commonly used at land-based intensive fish-far ms in Europe. Screen mesh pore sizes of 60-200 mu m are common. There is li ttle advantage in using pore sizes smaller than 60 mu m. Low concentration aquaculture solids usually settle discretely in sedimentation tanks, i.e. w ith no agglomeration of particles that would increase their settling veloci ty. Such basins are prone to many technical problems, and in most situation s are unlikely to be suitable for the treatment of solids in the primary wa stewater from aquaculture facilities. Sedimentation basins may be appropria te for secondary de-watering or thickening. Overflow rates of 1.0-2.7 m(3) m(-2) h(-1) have been reported. Bead filters and Rotation columns have been shown to perform well for solids removal in limited flow-rate recycle syst ems. The sludge produced by separation technology can be thickened and stab ilised by the addition of lime, to kill pathogenic diseases and restrict pu trefaction. The resulting sludge has been spread on agricultural land. (C) 2000 Elsevier Science B.V. All rights reserved.