Application of microbead biological filters

被引:34
作者
Timmons, MB [1 ]
Holder, JL
Ebeling, JM
机构
[1] Cornell Univ, Ithaca, NY 14853 USA
[2] JLH Consulting, Courtenay, BC, Canada
[3] Conservat Funds Freshwater Inst, Shepherdstown, WV USA
关键词
biological filter; microbead; data;
D O I
10.1016/j.aquaeng.2005.07.003
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The application of floating microbead filters to aquaculture is reviewed and discussed. The microbead filter is distinctly different from the more commonly used floating bead filters that are used today. Conventional bead filters work in pressured vessels and use a media that is only slightly buoyant. The required mass of beads for the volume required make the media a relatively expensive component of a floating bead filter in contrast to sand or microbead media that is much less expensive on a per volume basis. Microbead filters use polystyrene beads (microbead) that are 1-3 mm in diameter (floating bead filters use media approximately 3 mm in diameter also). Microbead have an overall bulk density of 16 kg/m(3) and a specific surface area of 3936 m(2)/m(3) (for I mm beads). This material can be obtained commercially in bulk for roughly US$ 4 kg(-1) of material. Biological filters that use microbeads for their nitrifying substrate can be thought of as a trickling bio-filter in terms of how the flow distribution and collection mechanics are designed and operated. For design purposes, microbead filters can be assumed to nitrify approximately 1.2 kg of TAN/m(3) of media per day for warm water systems with influent ammonia-nitrogen levels from 2 to 3 mg/l. For cool water applications, rates should be assumed to be 50% of warm water rates or use rates similar to those used for fluidized sand beds. Designs and results in several applications are presented. Microbead filters have been used successfully by several commercial growers after being first introduced in the mid 1990s. Effects of capitalization for equipment and buildings upon production costs is discussed and presented in graphical form. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:332 / 343
页数:12
相关论文
共 10 条
[1]  
CUNNINGHAM DL, 2003, U GEORGIA COOPERATIV, V1228
[2]  
EBELING JM, 2000, THESIS U MARYLAND
[3]   Evaluation of the nitrification rates of microbead and trickling filters in an intensive recirculating tilapia production facility [J].
Greiner, AD ;
Timmons, MB .
AQUACULTURAL ENGINEERING, 1998, 18 (03) :189-200
[4]  
PERRY C, 1991, MANPOWER MANAGEMENT, P20
[5]  
Summerfelt ST, 1996, T ASAE, V39, P1161, DOI 10.13031/2013.27608
[6]  
Summerfelt ST, 2004, P 5 INT C REC AQ VIR, P227
[7]  
Timmons M.B., 2002, Recirculating Aquaculture Systems, V2nd, P760
[8]  
*WATT PUBL, 1951, BROIL GROW STAT BROI
[9]   TEMPERATURE EFFECTS ON BIODRUM NITRIFICATION [J].
WORTMAN, B ;
WHEATON, F .
AQUACULTURAL ENGINEERING, 1991, 10 (03) :183-205
[10]   Effects of organic carbon on nitrification rate in fixed film biofilters [J].
Zhu, SM ;
Chen, SL .
AQUACULTURAL ENGINEERING, 2001, 25 (01) :1-11