Recombinant Microorganisms for Starch Processing

Through recombinant DNA technology, amylolytic yeast strains have been “con­structed.” This allows for the design of ethanol production processes, excluding the liquefaction and saccharification steps using exogenous enzymes, and the uti­lization of only one bioagent during the transformation, the yeast (consolidated bioprocessing, CBP). The savings obtained during the commercial implementa­tion of such a process could offset by far the lower growth rates and the longer fermentation times. In this way, a single microorganism can directly convert the starch into ethanol (Cardona and Sanchez, 2007). Some examples of these efforts are shown in Table 6.3. Lynd et al. (2002) mention, among the saccharolytic genes that have been introduced into microorganisms as S. cerevisiae and Klebsiella oxytoca, those encoding a-amylase, glucoamylase, amylopullulanase, pectate lyase, and polygalacturonase obtained from bacterial and fungal sources.

Many of the investigated recombinant strains have demonstrated the pro­duction of ethanol from starch, but in some cases, the results are not definitive. Surprisingly, reduced starch hydrolysis and fermentation rates have been observed for yeast strains expressing a set of genes previously considered as appropriate, as is the case of the work of Knox et al. (2004). This example shows the difficul­ties that arise during the research using recombinant microorganisms. Although the methods of genetic transformation are relatively developed, the results can be unexpected. This is a key factor when these microorganisms are evaluated from an industrial point of view. For this reason, deep studies on the effects of genetic modifications on engineered strains are required.

The processes with microorganisms modified by genetic engineering involve the optimization not only of microbial physiology parameters, but also of cell culture parameters (retention and stability of plasmids, nutritional factors, cell growth, and protein synthesis). Therefore, the modeling of these processes and the application of the principles of biochemical engineering can be helpful con­sidering the uncertainties and complexities inherent to these biological systems (Cardona and Sanchez, 2007). An example of this type of modeling is the work of Kobayashi and Nakamura (2004), who corroborated experimentally at laboratory scale the higher productivity of the continuous fermentation process from starch using recombinant yeast cells immobilized in calcium alginate beads in compari­son with the free cell system.

Another approach employed for modeling this process is the so-called flux balance analysis. Qakir et al. (2004) have employed and experimentally validated this methodology in the case of yeasts. They have determined that if the split ratio in the branch point of the glucose-6-phosphate corresponding to the glucolytic

Подпись:Some Examples of Recombinant Microorganisms with Potential Use for Fuel Ethanol Production

TABLE 6.3

Host

expressed enzymes

Gene Donor

feedstock/Medium

remarks

references

Saccharomyces

a-amylase

Bacillus subtilis

Starch-containing

Batch and fed-batch cultures;

Qakir et al. (2004); Altinta?

cerevisiae YPG/AB; S. cerevisiae YPG/G

Glucoamylase

Aspergillus awamori

medium

productivity 0.27-0.35 g/ (L. h); EtOH conc. 47.5 g/L (fed-batch); yield 0.46 g/g starch

et al. (2002); Ulgen et al. (2002)

S. cerevisiae YF207/ pGA11/pAA12

a-amylase

Glucoamylase

B. stearothermophilus Rhizopus oryzae

Low-temperature- cooked cornstarch

Batch culture; 36 h cultivation; EtOH conc. 18-30 g/L

Shigechi et al. (2004)

S. cerevisiae X1278b

a-amylase

Glucoamylase

Lipomyces kononenkoae Saccharomycopsis fibuligera

Starch-containing

medium

Batch culture; 120 h cultivation; EtOH conc. 21 g/L; yield 0.4 g/g starch; L. kononenkoae genes included promoter and terminator of S. cerevisiae PGK1

Knox et al. (2004)

S. cerevisiae SR96

Glucoamylase

S. diastaticus

Starch-containing

medium

Immobilized cells in calcium alginate; EtOH conc. 7.2 g/L; 200 h cultivation

Kobayashi and Nakamura

(2004)

Klebsiella oxytoca P2(pC46)

a-amylase

Pullulanase

B. stearothermophilus Thermoanaerobium brockii

Starch-containing

medium

EtOH conc. 15 g/L; yield 0.36-0.40 g/g starch

dos Santos et al. (1999)

Sacharomyces sp.

Xylose reductase

Pichia stipitis

1400(pLNH32);

Xylitol

P. stipitis

S. cereviskie CEN.

dehydrogenase

PK113-7D

Xylulokinase

S. cerevisiae

Zymomonas mobilis

Xylose isomerase

Escherichia <

ZM4(pZB5)

Xylulokinase

E. coli

Transketolase

E. coli

Transaldolase

E. coli

E. coli ATCC 9637,

Pyruvate

Z mobilis

ATCC 11303, ATCC

decarboxylase

15244

Alcohol

dehydrogenase

Z. mobilis

Glucose and xylose containing medium; acid pretreated starch industry effluents

 

Saccharomyces sp. strain is the product of fusion between S. diastaticus and S. uvarum and is capable of fermenting xylose to ethanol and utilizing it for aerobic growth; batch cultures; 48 h (sugars medium), 8 d (starch effluents) cultivation; EtOH cone. 60 g/L; yield 84%

Introduced genes codify xylose assimilation and metabolism; batch culture; 48 h cultivation; EtOH cone. 62 g/L

Hexose and pentose — assimilating E. coli acquires the ability for producing ethanol by introducing ethanol pathway genes; productivity 1.4 g/(L. h) from glucose. 0.64 g/(L. h) from xylose; EtOH cone. 41 g/L from xylose, 57 g/L from glucose; patented strain

 

Ho et al. (1998); Zaldivar et al. (2005)

 

Подпись: Microorganisms for Ethanol Production 145

Glucose and xylose containing medium

 

Leksawasdi et al. (2001)

 

Glucose or xylose containing medium

 

Ingram et al. (1991)

 

Continued

 

Подпись:Some Examples of Recombinant Microorganisms with Potential Use for Fuel Ethanol Production

TABLE 6.3 (Continued)

Host

expressed enzymes

Gene Donor

feedstock/Medium

remarks

references

E. coli FBR3

Pyruvate

decarboxylase

Alcohol

dehydrogenase

Z. mobilis Z. mobilis

Mixed sugars (glucose, xylose, arabinose)

Batch process; 72 h cultivation; EtOH conc. 44 g/L; yield 0.46-0.47 g/g; productivity 1.14 g/(L. h)

Dien et al. (1998)

Klebsiella oxytoca M5A1

Pyruvate

decarboxylase

Alcohol

dehydrogenase

Z. mobilis Z. mobilis

Crystalline cellulose

Native strain can uptake cellobiose and cellotriose; introduced genes codify ethanol pathway; batch SSF with reduced dosage of cellulases; EtOH conc. 47 g/L; yield 0.47 g/g cellulose

Ingram and Doran (1995)

Klebsiella oxytoca M5A1

Pyruvate decarboxylase Alcohol dehydrogenase 2 endoglucanases

Z. mobilis Z. mobilis

Erwinia chrysanthemi

Amorphous cellulose

Strain produced over 20,000 U/L endoglucanase and was able to ferment cellulose to ethanol; yield 58-76%; no addition of exogenous cellulases; potential strain for DMC of cellulose

Zhou and Ingram (2001)

Подпись: Microorganisms for Ethanol Production 147

S. cerevisiae L26126GC

Endo/exoglucanase

p-glucosidase

Bacillus sp. strain DO4 B. circulans

Crystalline cellulose

Batch SSF; 12 h cultivation; saccharolytic yeast capable of enzyme production; EtOH conc. 20.4 g/L; a considerable amount of commercial enzymes was reduced; potential strain for DMC of cellulose

Cho and Yoo (1999)

Clostridium

cellulolyticum

Pyruvate

decarboxylase

Alcohol

dehydrogenase

Z. mobilis

Cellulose

Native cellulolytic strategy

Guedon et al. (2002)

S. cerevisiae

Cellobiohydrolase

Thermoascus

aurantiacus

Crystalline cellulose

Recombinant cellulytic strategy

Hong et al. (2003)

 

metabolic pathway is changed by genetic manipulations, ethanol yield from starch can be considerably affected. This shows that the improvement in ethanol produc­tion goes with a rational design of metabolic pathways. In the future, this infor­mation could be crucial when different bioprocesses are designed, although it is necessary to analyze the costs and the complexity for acquiring this information in comparison with other “more traditional” procedures of design and control.

Similarly, important parameters, such as the stability of the plasmids used for introducing the desired traits to yeast cells, depend on the definition of the best environmental conditions during the cultivation of recombinant microorganisms. For example, Mete Altinta§ et al. (2002) showed that culture media containing specific salts and yeast extract drastically enhance plasmid stability during fed — batch cultures of yeasts using starch as feedstock.