scholarly journals The profile of enzymes relevant to solvent production during direct fermentation of sago starch by Clostridium saccharobutylicum P262 utilizing different pH control strategies

2008 ◽  
Vol 13 (1) ◽  
pp. 33-39 ◽  
Author(s):  
Madihah Md Salleh ◽  
Liew Shiau Tsuey ◽  
Arbakariya Bin Ariff
2002 ◽  
Vol 94 (2) ◽  
pp. 99-105 ◽  
Author(s):  
Mohamad Rosfarizan ◽  
Ariff Arbakariya ◽  
Mohd Ali Hassan ◽  
Mohamed Ismail Abdul Karim ◽  
Shimizu Hiroshi ◽  
...  

2001 ◽  
Vol 67 (11) ◽  
pp. 5127-5133 ◽  
Author(s):  
Ana M. López-Contreras ◽  
Hauke Smidt ◽  
John van der Oost ◽  
Pieternel A. M. Claassen ◽  
Hans Mooibroek ◽  
...  

ABSTRACT Growth and the production of acetone, butanol, and ethanol byClostridium beijerinckii NCIMB 8052 on several polysaccharides and sugars were analyzed. On crystalline cellulose, growth and solvent production were observed only when a mixture of fungal cellulases was added to the medium. On lichenan growth and solvent production occurred, but this polymer was only partially utilized. To increase utilization of these polymers and subsequent solvent production, the genes for two new glycoside hydrolases, celA and celD from the fungus Neocallimastix patriciarum, were cloned separately into C. beijerinckii. To do this, a secretion vector based on the pMTL500E shuttle vector and containing the promoter and signal sequence coding region of the Clostridium saccharobutylicum NCP262 eglA gene was constructed and fused either to the celA gene or thecelD gene. Stable C. beijerinckiitransformants were obtained with the resulting plasmids, pWUR3 (celA) and pWUR4 (celD). The recombinant strains showed clear halos on agar plates containing carboxymethyl cellulose upon staining with Congo red. In addition, their culture supernatants had significant endoglucanase activities (123 U/mg of protein for transformants harboring celA and 78 U/mg of protein for transformants harboring celD). AlthoughC. beijerinckii harboring either celA orcelD was not able to grow, separately or in mixed culture, on carboxymethyl cellulose or microcrystalline cellulose, both transformants showed a significant increase in solvent production during growth on lichenan and more extensive degradation of this polymer than that exhibited by the wild-type strain.


2012 ◽  
Vol 65 (2) ◽  
pp. 262-269 ◽  
Author(s):  
I. Mariakakis ◽  
J. Krampe ◽  
H. Steinmetz

A series of batch experiments investigating two different pH control strategies, initial pH adjustment and continuous pH control, have been carried out in large laboratory-scale reactors with working volumes of 30 L. In both cases, pH was varied between 5 and 7.5. Sucrose concentrations were also varied starting from 0 up to 30 g/L. Higher hydrogen production yields can be achieved by batch experiments through continuous pH control than by simple initial pH adjustment. In the case of continuous pH control, maximization of hydrogen yield was acquired for slightly acidic pH of 6.5. Continuous pH control in the neutral pH range of 7.0 and in pH lower than 6.5, induced a reduction in the hydrogen production yield. Sucrose can be completely degraded only for a pH higher than 6. Lower pH values seem to inhibit the hydrogen-producing bacteria. Under the conditions of continuous pH adjustment at pH 6.5 and a sucrose concentration of 25 g/L the maximum hydrogen yield of 1.79 mol H2/mol hexose was obtained. These conditions could be applied for the batch start-up of large fermentors.


1994 ◽  
Vol 30 (4) ◽  
pp. 159-168 ◽  
Author(s):  
Ibrahim A. AI-Ghusain ◽  
Jason Huang ◽  
Oliver J. Hao ◽  
Bong S. Lim

The alternating aerobic-anoxic (AAA) process offers many advantages for wastewater treatment and sludge digestion. Laboratory scale experiments were conducted to investigate the feasibility of using pH as a realtime control parameter for this process. Several well defined control points on the pH curve were identified, e.g., ammonia valley and nitrate apex. These points were directly related to the alternating nitrification and denitrification reactions in the process, and were found to be consistent with those previously identified using ORP. Although both pH and ORP can be used as real-time control parameters, pH provides several additional advantages over ORP. Based on these findings, real-time control strategies (fixed pH setpoints and dynamic pH control) were developed and tested. Results from laboratory scale AAA sludge digestion using fixed pH setpoints (6-8) indicated that 36% MLVSS reduction, 39% TN reduction and almost 48% saving in aeration energy was achieved after 300 hrs of digestion.


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