This work reports the results of the first worldwide full scale application of the concept of MBBTF (moving bed bio trickling filter) applied to biological gas treatment. A full scale prototype of an innovative MBBTF for for gaseous effluents treatment was designed and installed in a tannery wastewater treatment plant (Cuoiodepur, Pisa, Italy). The prototype was operated for 9 months with empty bed retention time of 3.5 s and treated 8000 m3 h–1 of a gaseous stream with a concentration of hydrogen sulphide up to 300 mg S m–3 (in average 170 mg S m–3). The removal efficiency was on average 80% and the highest elimination capacity (EC) was 18 kg S-H2S d–1 (corresponding to a specific EC of 90 g H2S m–3 bed h–1). The rotation of the bed was demonstrated to be a suitable solution to promote the detachment of the biomass and, thus, to control the pressure headlosses caused by the biofilm growth. The start up phase lasted 2 weeks and, the role of several process parameters (including pH, recirculated water flow rate and rotation frequency) was evaluated.
Moving Bed BioTrickling Filters: an innovative solution for hydrogen sulphide removal from gas streams / Spennati, Francesco; Mannucci, Alberto; Mori, Gualtiero; Giordano, Cesira; Munz, Giulio.. - In: DESALINATION AND WATER TREATMENT. - ISSN 1944-3986. - ELETTRONICO. - 61:(2017), pp. 215-221. [10.5004/dwt.2016.11138]
Moving Bed BioTrickling Filters: an innovative solution for hydrogen sulphide removal from gas streams
SPENNATI, FRANCESCO;MANNUCCI, ALBERTO;MUNZ, GIULIO
2017
Abstract
This work reports the results of the first worldwide full scale application of the concept of MBBTF (moving bed bio trickling filter) applied to biological gas treatment. A full scale prototype of an innovative MBBTF for for gaseous effluents treatment was designed and installed in a tannery wastewater treatment plant (Cuoiodepur, Pisa, Italy). The prototype was operated for 9 months with empty bed retention time of 3.5 s and treated 8000 m3 h–1 of a gaseous stream with a concentration of hydrogen sulphide up to 300 mg S m–3 (in average 170 mg S m–3). The removal efficiency was on average 80% and the highest elimination capacity (EC) was 18 kg S-H2S d–1 (corresponding to a specific EC of 90 g H2S m–3 bed h–1). The rotation of the bed was demonstrated to be a suitable solution to promote the detachment of the biomass and, thus, to control the pressure headlosses caused by the biofilm growth. The start up phase lasted 2 weeks and, the role of several process parameters (including pH, recirculated water flow rate and rotation frequency) was evaluated.File | Dimensione | Formato | |
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