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PNNL-13501 - Pacific Northwest National Laboratory

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carbohydrate value from the corn fiber, including the<br />

glucose from hydrolysis of the cellulose fraction. In this<br />

project, selective hydrolysis was evaluated to recover<br />

monosaccharides from the hemicellulosic component.<br />

Development of Novel and Simple Processing Strategies<br />

Based in part on the literature and on testing both under<br />

this project and under a separate LDRD project led by<br />

James Franz, three hydrolysis processing strategies were<br />

developed, and portions of the processing strategies were<br />

further tested (see Figure 2).<br />

Corn<br />

Fiber<br />

Corn<br />

Fiber<br />

Corn<br />

Fiber<br />

(Step 1) (Step 2)<br />

Prehydrolysis<br />

(Thermochemical)<br />

Hydrolysis<br />

(Enzymatic)<br />

Prehydrolysis (Step 1) and Enzymatic Hydrolysis (Step 2)<br />

1-Step Hydrolysis<br />

(Step 1)<br />

Hydrolysis<br />

(Thermochemical)<br />

Prehydrolysis<br />

(Thermochemical)<br />

2-Step (Thermochemical) Hydrolysis<br />

Filtration<br />

(Step 1) (Step 2)<br />

Optional<br />

Separations<br />

Step(s)<br />

Filtration<br />

Residual Solids<br />

(To Upgraded Livestock Feed)<br />

C-5’s and C-6’s<br />

(To Product Conditioning/<br />

Catalytic Conversion or Fermentation)<br />

Hydrolysis<br />

(Thermochemical)<br />

Figure 2. Hydrolysis processing strategies<br />

Residual Solids<br />

(To Upgraded Livestock Feed)<br />

C-5’s and C-6’s<br />

(To Product Conditioning/<br />

Catalytic Conversion or Fermentation)<br />

Filtration<br />

Residual Solids<br />

(To Upgraded Livestock Feed)<br />

C-5’s and C-6’s<br />

(To Product Conditioning/<br />

Catalytic Conversion<br />

or Fermentation)<br />

The first approach included both acid and enzyme<br />

hydrolysis. The fiber was first subjected to selective acid<br />

hydrolysis to solubilize the hemicellulosic fraction of the<br />

corn fiber. Next, enzymes were added to further break<br />

down the solubilized hemicellulosic fraction to the<br />

monomers. (An alternative to this flowsheet is to conduct<br />

two acid hydrolysis steps, the first to solubilize the<br />

hemicellulosic fraction, with a filtration to remove the<br />

solids, and the second hydrolysis to convert the<br />

oligosaccharides in solution to monosaccharides. With<br />

this approach, however, the conditions of the second<br />

hydrolysis were needed to control and prevent the<br />

formation of degradation products.)<br />

The second approach involved a one-step acid hydrolysis<br />

at selected conditions. This approach was simpler than<br />

the first; however, if the conditions were not right, total<br />

conversion to the monosaccharides did not occur, or<br />

degradation products could form.<br />

The third approach used a two-step thermochemical<br />

method. In the first step, the hemicellulose component<br />

was solubilized, and an optional polishing step was<br />

employed to remove the monosaccharides (e.g.,<br />

440 FY 2000 <strong>Laboratory</strong> Directed Research and Development Annual Report<br />

ultrafiltration), then the slurry was subjected to further<br />

hydrolysis to break down the oligosaccharides to the<br />

monomers. By removing the monosaccharides after the<br />

first hydrolysis, the formation of degradation products<br />

was minimized, while monosaccharide production is<br />

maximized.<br />

Acid Hydrolysis Testing<br />

During evaluation of some of the acid hydrolysis<br />

conditions, significant solubilization was observed<br />

without the formation of degradation products. This<br />

testing was conducted at the micro-scale and bench-scale.<br />

The bench-scale results illustrated in Figure 3 were<br />

obtained by operation at elevated temperatures without<br />

acid addition. Even without acid addition, approximately<br />

25% solubilization took place, with the solubilized<br />

fraction mainly consisting of oligomers. At higher<br />

temperatures, significantly more solubilization took place,<br />

but degradation products also formed. The micro-scale<br />

testing (Figure 3) was conducted under selective<br />

hydrolysis conditions with the addition of acid.<br />

Approximately 50% solubilization took place, and no<br />

degradation products (e.g., furfural) were detected.<br />

Approximately half of the solubilized fraction was<br />

monosaccharides, and the remainder was<br />

oligosaccharides.<br />

Corn Fiber Solubilized (%)<br />

70<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

Bench-scale Testing Results<br />

Operation without acid at lower temperatures<br />

Operation at low temperatue with acid addition<br />

allows for approximately 25% solubilization<br />

allows for approximately 50% solubilization<br />

(Mostly as soluble oligomers) (25% soluble sugars and 25% soluble oligomers, no detectable furfural)<br />

Increasing Temperature<br />

Shorter Hold Time Longer Hold Time<br />

Enzyme Hydrolysis Testing<br />

Micro-scale Kinetic Testing Results<br />

Enzyme hydrolysis testing was conducted, using several<br />

commercially available enzymes. These enzymes are<br />

relatively inexpensive and readily available. As can be<br />

seen in Figure 4, three of the enzymes tested showed<br />

promise for converting hemicellulose to the monomer<br />

sugars (xylose and arabinose). In these tests, the corn<br />

fiber itself was treated with the enzymes. If the corn fiber<br />

were first treated via selective thermochemical (with or<br />

%Yield, g/g Fiber<br />

10<br />

9<br />

8<br />

7<br />

6<br />

5<br />

4<br />

3<br />

2<br />

1<br />

0<br />

Increasing Hold Time<br />

Arabinose<br />

Galactose<br />

Xy lose<br />

Glucose<br />

(a): Micro-scale kinetic testing results<br />

provided by Jim Franz and Miikhail Alnajjar<br />

Figure 3. Acid/thermochemical hydrolysis of corn fiber

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