202-210<span style="font-size:11.0pt;line-height:115%;
font-family:" calibri","sans-serif";mso-ascii-theme-font:minor-latin;mso-fareast-font-family:="" "times="" new="" roman";mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:="" minor-latin;mso-bidi-font-family:"times="" roman";mso-ansi-language:en-us;="" mso-fareast-language:en-us;mso-bidi-language:ar-sa"="">The use of a biological
reactor (bioreactor) as a means of removing hydrogen sulfide from waste water
and converting it to elemental sulfur has several advantages over conventional
physical/chemical treatment processes. A suspended-growth continuous-flow stirred-tank
bioreactor utilizing the green sulfur bacterium Chlorobium limicola was
successfully operated at five different sulfide loading rates and three
different hydraulic retention times. In all but one of the five experiments,
the rate of consumption of the sulfide was equal to its loading rate. The
separation of elemental sulfur from the bioreactor contents is essential to
realize its value as a chemical industry feedstock. Separations of elemental
sulfur by plain settling, settling at elevated p<span style="font-size:11.0pt;line-height:
115%;font-family:" calibri","sans-serif";mso-ascii-theme-font:minor-latin;="" mso-fareast-font-family:"times="" new="" roman";mso-fareast-theme-font:minor-fareast;="" mso-hansi-theme-font:minor-latin;mso-bidi-font-family:arial;mso-ansi-language:="" en-us;mso-fareast-language:en-us;mso-bidi-language:ar-sa;mso-bidi-font-style:="" italic"="">H, <span style="font-size:11.0pt;line-height:115%;
font-family:" calibri","sans-serif";mso-ascii-theme-font:minor-latin;mso-fareast-font-family:="" "times="" new="" roman";mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:="" minor-latin;mso-bidi-font-family:"times="" roman";mso-ansi-language:en-us;="" mso-fareast-language:en-us;mso-bidi-language:ar-sa"="">filtration and centrifuging
were tested at bench scale using the contents of several batch bioreactors.
Under plain settling, elemental sulfur and bacteria were removed from
suspension to the same degree. Raising the <span style="font-size:
11.0pt;line-height:115%;font-family:" calibri","sans-serif";mso-ascii-theme-font:="" minor-latin;mso-fareast-font-family:"times="" new="" roman";mso-fareast-theme-font:="" minor-fareast;mso-hansi-theme-font:minor-latin;mso-bidi-font-family:arial;="" mso-ansi-language:en-us;mso-fareast-language:en-us;mso-bidi-language:ar-sa"="">pH to <span style="font-size:11.0pt;
line-height:115%;font-family:" calibri","sans-serif";mso-ascii-theme-font:minor-latin;="" mso-fareast-font-family:"times="" new="" roman";mso-fareast-theme-font:minor-fareast;="" mso-hansi-theme-font:minor-latin;mso-bidi-font-family:arial;mso-ansi-language:="" en-us;mso-fareast-language:en-us;mso-bidi-language:ar-sa"="">8.6 or <span style="font-size:11.0pt;
line-height:115%;font-family:" calibri","sans-serif";mso-ascii-theme-font:minor-latin;="" mso-fareast-font-family:"times="" new="" roman";mso-fareast-theme-font:minor-fareast;="" mso-hansi-theme-font:minor-latin;mso-bidi-font-family:arial;mso-ansi-language:="" en-us;mso-fareast-language:en-us;mso-bidi-language:ar-sa"="">8.8 resulted in some of the sulfur or bacteria
settling independently of the sulfur-bacteria floes. Filtration was found to
give conflicting results with different batches of bacteria. Centrifugation
resulted in the best separation between elemental sulfur and bacteria; 90% of
the elemental sulfur and 29% of the bacteria could be removed from suspension.</span