05.06.2013 Views

PNNL-13501 - Pacific Northwest National Laboratory

PNNL-13501 - Pacific Northwest National Laboratory

PNNL-13501 - Pacific Northwest National Laboratory

SHOW MORE
SHOW LESS

Create successful ePaper yourself

Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.

Concentration (g/100g solution)<br />

Concentration (g/100g solution)<br />

0.80<br />

0.70<br />

0.60<br />

0.50<br />

0.40<br />

0.30<br />

0.20<br />

0.10<br />

0.00<br />

2.50<br />

2.00<br />

1.50<br />

1.00<br />

0.50<br />

0.00<br />

without acid) hydrolysis (i.e., as in Figure 3), and the<br />

hydrolysate were subjected to enzymatic treatment, the<br />

enzymes would likely be even more effective because<br />

mass transfer limitations and accessibility to the<br />

hemicellulosic fraction would be minimized.<br />

Processing Equipment<br />

Xylose Concentrations<br />

A B C D E Control<br />

Enzyme<br />

Glucose Concentrations<br />

Based on observations during testing and filtration, and<br />

the characteristics of the feed slurry, bench-scale<br />

processing equipment was developed and modification of<br />

an existing continuous flow system was initiated. A<br />

Moyno feed pump, capable of pumping the feed slurry at<br />

the conditions evaluated was also acquired. In addition,<br />

since the acid hydrolysis was conducted at slightly<br />

elevated pressure (to keep the reaction mixture in the<br />

liquid phase), pressure letdown was required for the<br />

continuous system. It has been observed, however, that if<br />

the pressure is reduced through a small orifice or<br />

instantaneously, the fiber particles break apart and are<br />

more difficult to filter. Thus, a more amenable pressure<br />

letdown system has been designed, and the hardware for<br />

the system has been acquired.<br />

Summary and Conclusions<br />

Shortest Time<br />

Medium Ti me<br />

Longest Ti me<br />

A B C D E Control<br />

Enzyme<br />

Figure 4. Enzyme hydrolysis of corn fiber<br />

Shortest Time<br />

Medium Ti me<br />

Longest Ti me<br />

The hemicellulosic fraction of corn fiber is a promising<br />

source for providing 5-carbon sugars that can be<br />

converted to value-added products. Observations from<br />

Concentration (g/100g solution)<br />

Concentration (g/100g solution)<br />

0.70<br />

0.60<br />

0.50<br />

0.40<br />

0.30<br />

0.20<br />

0.10<br />

0.00<br />

0.70<br />

0.60<br />

0.50<br />

0.40<br />

0.30<br />

0.20<br />

0.10<br />

0.00<br />

Arabinose Concentrations<br />

A B C D E Control<br />

Enzyme<br />

Mannose/Fructose Concentrations<br />

Shortest Time<br />

Medium Ti me<br />

Longest Time<br />

Shortest Time<br />

Medium Ti me<br />

Longest Time<br />

A B C D E Control<br />

Enzyme<br />

the tests using acid and enzyme hydrolysis to recover the<br />

hemicellulosic fraction are summarized below:<br />

• Some hydrolysis options have been developed from<br />

literature and test results. Based on the data to date,<br />

one of the most attractive approaches is a two-step<br />

process, using acid and enzyme hydrolysis. The data<br />

suggest that this approach will result in high yields of<br />

monosaccharides while minimizing formation of<br />

degradation products.<br />

• Thermochemical (with and without acid addition)<br />

hydrolysis conditions have been identified, where<br />

significant corn fiber solubilization takes place and<br />

little or no degradation products are formed.<br />

• Commercially available and relatively inexpensive<br />

enzymes have been identified that are effective in<br />

converting corn fiber hemicellulose to xylose and<br />

arabinose.<br />

• Bench-scale equipment was developed for continuous<br />

thermochemical processing. The equipment was<br />

selected based on observations made during the<br />

testing.<br />

Separations and Conversions 441

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!