Electrochemical pH Control and Carbon Supply for Microalgae Cultivation

2021 ◽  
pp. 131796
Author(s):  
Ga-Yeong Kim ◽  
Jina Heo ◽  
Kwiyong Kim ◽  
Jane Chung ◽  
Jong-In Han
1991 ◽  
Vol 83 (3) ◽  
pp. 331-338 ◽  
Author(s):  
Per-Olof Lundquist ◽  
Kerstin Russ-Danell
Keyword(s):  

2018 ◽  
Author(s):  
Sahan Dissanayake ◽  
Randall A. Bluffstone ◽  
E. Somanathan ◽  
Harisharan Luintel ◽  
N. S. Paudel ◽  
...  

2007 ◽  
Vol 61 (3) ◽  
pp. 305-309
Author(s):  
Takayuki Ohkura
Keyword(s):  

Author(s):  
marcelo rudek ◽  
Osiris Canciglieri Junior ◽  
bruno miyawaki ◽  
Thiago Carvalho de Mello ◽  
Tiago Francesconi

1998 ◽  
Vol 38 (4-5) ◽  
pp. 273-280 ◽  
Author(s):  
A. G. Werker ◽  
E. R. Hall

Spectra of microbial fatty acid methyl esters were used to assess the influence of pH on the biofilm and suspended biomass populations within bench scale moving bed bioreactors treating bleached kraft mill effluent. The fatty acid spectral data were reduced by logcontrast canonical component analysis. The first canonical component differentiated biofilm from suspended populations and the second two appeared to indicate an influence of pH on microbial ecology. Thus, the biofilm and suspended microbial communities were distinct, as were the populations acclimated at pH 6 and pH 8. Experimental data for total organic carbon removal suggested that the more recalcitrant fraction of the influent was consumed by the slower growing, high SRT biofilm fraction of the biomass. Since the biofilm ecology was sensitive to pH within typical pH operating limits of full-scale systems, tighter pH control might improve treatment reliability in the event of process transients.


1998 ◽  
Vol 38 (4-5) ◽  
pp. 29-35 ◽  
Author(s):  
C. J. Banks ◽  
P. N. Humphreys

The stability and operational performance of single stage digestion with and without liquor recycle and two stage digestion were assessed using a mixture of paper and wood as the digestion substrate. Attempts to maintain stable digestion in both single stage reactors were unsuccessful due to the inherently low natural buffering capacity exhibited; this resulted in a rapid souring of the reactor due to unbuffered volatile fatty acid (VFA) accumulation. The use of lime to control pH was unsatisfactory due to interference with the carbonate/bicarbonate equilibrium resulting in wide oscillations in the control parameter. The two stage system overcame the pH stability problems allowing stable operation for a period of 200 days without any requirement for pH control; this was attributed to the rapid flushing of VFA from the first stage reactor into the second stage, where efficient conversion to methane was established. Reactor performance was judged to be satisfactory with the breakdown of 53% of influent volatile solids. It was concluded that the reactor configuration of the two stage system offers the potential for the treatment of cellulosic wastes with a sub-optimal carbon to nitrogen ratio for conventional digestion.


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