Cellulose & lignin
Wood, cellulose and recalcitrance
The microfibril-and-matrix architecture of wood, why recalcitrance is a design feature rather than a defect, and why the kraft process dominates despite burning roughly half the wood and the aromatic value of its lignin.
Wood is a composite in the strict engineering sense: crystalline cellulose microfibrils carry the load, and an amorphous matrix of hemicellulose and lignin binds them, distributes stress and keeps water where it belongs. The cellulose chains are β-1,4-linked glucose, thousands of units long; lying side by side, they are locked by hydrogen bonds into crystalline domains a few nanometres across — the microfibril that nanocellulose production isolates. Stiffness is set at this level: the elastic modulus of crystalline cellulose is of the order of a hundred gigapascals, comparable to structural metals, and it is the reinforcing phase for everything a tree builds. Softwood runs roughly 40–45% cellulose by mass, a quarter to a third hemicellulose — short, branched polysaccharides of five- and six-carbon sugars with no crystallinity — and a quarter to a third lignin, a cross-linked network of phenylpropanoid units assembled with no repeating pattern.
Why recalcitrance exists
A standing tree is a water transport system and a sugar store, and the cell wall evolved to protect the sugar from everything else. Lignin is the keystone of that defence: it is hydrophobic, fills the space between microfibrils and dominates the middle lamella, and shields the polysaccharides from hydrolytic enzymes — large proteins that need hydrated access to their substrate. An enzyme can cut a hemicellulose chain hanging free; it cannot pass through a lignified wall. Recalcitrance is therefore a design feature, not an accident. For industry it has one consequence: to free the cellulose you must break bonds in the matrix faster than you damage the fibre you are freeing. Every pulping process is an exercise in that selectivity, and each one fails where delignification stops being selective.
Why kraft wins
The kraft process, patented in 1879, cooks chips in white liquor — sodium hydroxide plus sodium sulfide. Hydroxide and hydrosulfide ions cleave the ether linkages holding the lignin network together, above all the abundant β-O-4 aryl ethers; the fragments ionise as phenolates and dissolve, and much of the hemicellulose hydrolyses away. The chemistry alone does not explain the dominance; the recovery loop does. The spent liquor — black liquor, carrying the dissolved lignin and degraded carbohydrates — is concentrated and burned in a recovery boiler: the organics supply the mill’s steam and power, and the inorganic smelt is re-causticised with lime back into white liquor. A kraft mill runs on its own waste stream, which is why the overwhelming majority of the world’s chemical pulp is kraft pulp and why the process has outlived every challenger, including cleaner ones.
What it costs
The loop’s economy explains the losses. Yield is roughly half the dry wood: in hot alkali the reducing ends of polysaccharide chains unzip one unit at a time — the peeling reactions — and the lost carbohydrate burns with the lignin. Energy self-sufficiency and yield loss are one phenomenon seen from two sides. Meanwhile the lignin, the largest renewable reservoir of aromatics, is consumed as low-grade fuel rather than recovered as molecules — the problem the lignin chemistry page takes up. Residual lignin also darkens the pulp, so bleaching follows, with its own chemistry and its enzyme-assisted shortcuts. What kraft cannot do is raise selectivity at will: cook harder and you eat the cellulose; cook softer and bleach-plant yield collapses. That trade-off, not a missing invention, is what holds the industry in place.