EGEE 439
Alternative Fuels from Biomass Sources

5.3c Neutral pH Pretreatment

Pretreatment can also take place in neutral pH water. There are two pathways that can occur. One is when acidic compounds are released from acetylated hemicellulose, mainly acetic acid. This is also called autohydrolysis. Water can also dissociate as the temperature and pressure increases to near the supercritical point (approximately 374°C, 3200 psi), into H+ and OH−, and as this happens, the water behaves like an acid/base system. It is done in water without added chemicals, either in liquid hot water, steam explosion, or water near the supercritical point. The key parameters are time, temperature, and moisture content, and the effects are similar to low pH methods. A schematic for liquid hot water processing is shown in Figure 5.18.

 Liquid hot water process flow diagram
Figure 5.18: Liquid hot water process flow diagram*.
Credit: BEEMS Module B1

One process, developed by Inbicon, is a counter-current multi-stage hot water pretreatment process. There is a pilot-scale unit at Skærbæk, Denmark. It is a three-stage process using hot water (hydrothermal) at 80°C, 160-200 °C, and 190-230°C. After the first stage, liquid composed C5-molasses (sugar) is taken out of the process, which is used for animal feed. After the third stage, the fiber fraction contains cellulose and lignin. Bioethanol and a solid fuel for heat and power are produced when using enzymes, yeast, and fermentation. Figure 5.19 shows the before and after pretreatment of wheat straw (the raw wheat straw and the cellulosic-lignin portion).

 Pretreatment of wheat straw, before and after
Figure 5.19: Pretreatment of wheat straw, before and after.
Credit: BEEMS Module B1

The next pretreatment processes to discuss are at high pH. The high pH removes the lignin portion of biomass through the breaking of ether linkages (R-O-R’) that hold aromatic phenolic compounds together; ring opening can also take place. It is a depolymerization process. There are several processes and bases used, including: lime, calcium carbonate, potassium hydroxide, sodium hydroxide, and aqueous ammonia. Key parameters include temperature, reaction time, concentration of base, moisture of the feed material, as well as oxidizing agents. The effects include removal of most of the lignin, some removal of hemicellulose, and removal of acetyl links between lignin and hemicellulose.

Lignin is most prominent in grasses and woody biomass. It composes 6-35% of lignocellulosic biomass, depending on the type of grass or wood. Lignin is comprised of crosslinked, branched, monoaromatic units with methoxy and propyl alcohol functional groups. These are shown in Figure 5.20a. Figure 5.20b shows a model of a lignin molecule and how the aromatic monomers are linked together.

 Aromatic monomer alcohols of building blocks for lignin
Figure 5.20a: Aromatic monomer alcohols of building blocks for lignin.
Credit: Bembenic, Meredith, “The chemistry of subcritical water reactions of a hardwood derived lignin and lignin model compounds with nitrogen, hydrogen, carbon monoxide and carbon dioxide,” PhD Thesis, PSU, 2011
 Alder model of lignin representative molecule
Figure 5.20b: Alder model of lignin representative molecule.
Credit: Bembenic, Meredith, “The chemistry of subcritical water reactions of a hardwood derived lignin and lignin model compounds with nitrogen, hydrogen, carbon monoxide and carbon dioxide,” PhD Thesis, PSU, 2011