ANAEROBIC TREATMENT OF SALINE WASTEWATERS UNDER HIGH SULFIDE AND AMMONIA CONTENT

Citation
F. Omil et al., ANAEROBIC TREATMENT OF SALINE WASTEWATERS UNDER HIGH SULFIDE AND AMMONIA CONTENT, Bioresource technology, 54(3), 1995, pp. 269-278
Citations number
45
Categorie Soggetti
Energy & Fuels","Biothechnology & Applied Migrobiology",Agriculture
Journal title
ISSN journal
09608524
Volume
54
Issue
3
Year of publication
1995
Pages
269 - 278
Database
ISI
SICI code
0960-8524(1995)54:3<269:ATOSWU>2.0.ZU;2-7
Abstract
The anaerobic treatment of wastewaters from the seafood-processing ind ustry was studied in a 15 m(3) industrial pilot-plant. These effluents have a high organic content (10-60 g COD/litre), with protein percent ages between 25 and 70%, and a salinity similar to sea water: sodium ( 5-12 g/l), chloride (8-19 g/l) and sulphate (0 . 6-2 . 7 g/l). This hi gh concentration of salts, together with the production of sulphide an d ammonia due to sulphate reduction and protein breakdown, respectivel y, produces important inhibitory/toxic effects on non-adapted biomass. A mixture of anaerobic sludges from the treatment of non-saline waste waters was used as the inoculum. After an initial start-up procedure, where the acclimation of the biomass was the objective, 70-90% organic matter removal was achieved, operating at dissolved sulphide (DS) tot al ammonia (TA) and sodium concentrations in the ranges of 0 . 25-0 . 5 g S-DS/l, 1 . 0-3 . 0 g N-TA/l and 6-10 g/l, respectively. The adapt ation of the biomass to the salinity and the antagonistic effects on s odium toxicity caused by the presence of other ions made it possible t o operate at these high sodium concentrations. Due to the strong buffe ring capacity of the process, pH was maintained above 7 . 25, resultin g in levels of free hydrogen sulphide (FS) that were lower than 100 mg S-FS/l, which were not high enough to produce inhibition effects on a dapted sludges. However the control of the influent protein content is necessary, since values higher than 200 mg N-FA/l of free ammonia (FA ) were shown to be inhibitory for this process.