Efficient methods and compositions for recovery of products from organic acid pretreatment of plant materials
The invention is directed to compositions and processes concerning efficient downstream processing of products derived from organic acids pretreatment of plant materials.
1. A method of recovering lignin from a lignin suspension produced from a concentrated extraction liquor with a dry matter content of about 50 to about 65% derived from organic acids pretreatment of plant material, the method comprising the steps of:
a) separating lignin from the lignin suspension, wherein the lignin is separated by centrifugation with a centrifuge thereby forming a separated lignin and a first centrifugate, and
b) cleaning the separated lignin in the centrifuge by multiple applications of wash solution onto the separated lignin during centrifugation, to form at least a second and third centrifugate, wherein the multiple applications of wash solution comprise a sequential application starting with a first application of a wash solution comprising a first organic acids content washing water, and a second application of a wash solution comprising a second organic acids content washing water, wherein the organic acids content in the first organic acids content washing water is greater than the organic acids content in the second organic acids content washing water, and
c) recovering the first centrifugate and the second centrifugate for use in hemicellulosic juice concentration, and
d) recycling the third centrifugate for producing the lignin suspension in step a) by mixing the third centrifugate with the concentrated extraction liquor, and
e) discharging the separated lignin from step b) from the centrifuge.
2. The method according to claim 1 , wherein the centrifuge is a scraper centrifuge.
3. The method according to claim 1 , wherein the centrifuge is equipped with a spraying device for delivering wash solution.
4. The method according to claim 1 , wherein the centrifuge rotates continuously through the entire method.
5. The method according to claim 1 , wherein the wash solution comprises formic acid, acetic acid, and water.
6. The method according to claim 5 , wherein the wash solution has a content of formic acid of greater than 0% and up to 30% by weight.
7. The method according to claim 5 , wherein the wash solution has a content of acetic acid of greater than 0% and up to 20% by weight.
8. The method according to claim 1 , wherein the wash solution consists solely of water.
9. The method according to claim 1 , wherein the multiple applications of wash solution comprise a sequential application starting with a first application of a wash solution with an organic acid content of 0.5% to 10% by weight, a second application of a wash solution with an organic acid content of 0.2% to 1% by weight, and a final application of a wash solution comprised of fresh water.
10. The method according to claim 1 , wherein the first centrifugate is comprised of liquids separated from the lignin suspension applied to the centrifuge.
11. The method according to claim 1 , wherein the second centrifugate is comprised of a first wash solution comprised in the multiple applications of wash solution applied to the separated lignin in the centrifuge.
12. The method according to claim 1 , wherein the first and second centrifugates are collected and used for hemicellulosic juice production.
13. The method according to claim 1 , wherein the third centrifugate is comprised of a second and any subsequent wash solutions comprised in the multiple applications of wash solution applied to the separated lignin in the centrifuge.
14. The method according to claim 1 , wherein the third centrifugate is recycled to a lignin precipitation process that forms the lignin suspension applied to the centrifuge in a subsequent cycle of the method.
15. The method according to claim 1 , wherein the first centrifugate comprises 10% to 60% of the total centrifugates.
16. The method according to claim 1 , wherein the second centrifugate comprises 10% to 30% of the total centrifugates.
17. The method according to claim 1 , wherein the third centrifugate comprises 10% to 50% of the total centrifugate.
18. The method according to claim 1 , wherein the separated lignin from step e) is 90% to 99% pure, based on the total weight of the separated lignin from step e).