Processes for recovery of derivatives of native lignin
The present disclosure relates to processes for recovery of derivatives of native lignin from lignocellulosic feedstocks wherein the derivatives have a certain aliphatic hydroxyl content. Surprisingly, it has been found that stable and predictable antioxidant activity is provided by selecting for derivatives of native lignin having a certain aliphatic hydroxyl content.
1. A process for recovering a lignin derivative from a feedstock comprising softwood biomass, the lignin derivative having an aliphatic hydroxyl content of 7.0 mmol/g or less, the process comprises the steps of:
pulping the feedstock with a selected organic solvent (ETHANOL) supplemented with a selected acid catalyst (pH) for a selected period of time (TIME) at a selected temperature (TEMPERATURE) to produce a cellulosic solids fraction and an extractives liquid fraction;
separating the cellulosic solids fraction from the extractives liquid fraction; and
recovering the lignin derivative from the extractives liquid fraction, wherein softwood feedstock comprises Picea spp., Pinus spp., and combinations/hybrids thereof.
2. The process according to claim 1 , wherein the softwood feedstock comprises Picea spp. and the parameters ETHANOL, pH, TIME, and TEMPERATURE are selected to satisfy the equation: 65.2341−0.689028*Temperature+0.170969*Ethanol+0.0217104*pH*Temperature−0.0267202*pH*Ethanol−0.000116382*Time*Temperature+0.000382542*Time*Ethanol+0.00156337*Temperature*Temperature−0.00113549+Ethanol*Ethanol≦7 mmol/g.
3. The process according to claim 2 , wherein the recovered lignin derivative falls within the graphical representation of FIG. 4 .
4. The process according to claim 1 , wherein the softwood feedstock is a Pinus radiata spp. and the parameters ETHANOL, pH, TIME, and TEMPERATURE are selected to satisfy the equation: 44.4758−17.3944*pH−0.342106*Temperature+0.373582*Ethanol−0.0133583*pH*Time+0.124198*pH*Temperature+0.000205204*Time*Time−0.00333743*Ethanol*Ethanol≦7 mmol/g.
5. The process according to claim 4 , wherein the recovered lignin derivative falls within the graphical representation of FIG. 5 .
6. The process according to claim 1 , wherein the softwood feedstock is a Pinus taeda spp. and the parameters ETHANOL, pH, TIME, and TEMPERATURE are selected to satisfy the equation: 19.7852−11.2196*pH−0.153691*Time−2.39789*pH*pH+0.0880747*pH*Time+0.102069*pH*Temperature+0.0203294*pH*Ethanol−0.000537328*Time*Time−0.000706365*Temperature*Temperature−0.000470555*Ethanol*Ethanol≦7 mmol/g.
7. The process according to claim 6 , wherein the recovered lignin derivative falls within the graphical representation of FIG. 6 .