Solvent pulping process

Claim 2

In a solvent extraction pulping process wherein lignin is extracted from subdivided fibrous plant material by contacting said material at an elevated pulping temperature and pressure with a solvent pulping liquor comprising an aqueous solution of a lower aliphatic alcohol, the improvement which comprises providing a plurality of batch extractors and carrying out the following sequential steps in each extractor: (a) feeding a first charge of said subdivided fibrous plant material to a first extractor; (b) filling said first extractor with a first used pulping liquor so as to displace air from said first extractor; (c) introducing a second used pulping liquor of relatively high dissolved solids content at an elevated temperature and pressure into said first extractor so as to displace said first used pulping liquor, and recirculating said second used pulping liquor without separation of lignin at a relatively high velocity through said first extractor and through an external heat exchanger so as to effect rapid heating of said first charge to a predetermined pulping temperature of from about 160° to about 220° C. within not more than about 10 minutes at a predetermined pulping pressure of from about 10 to about 50 atmospheres, said second used pulping liquor being obtained from step (e), as hereinafter described, during pulping of another charge in a second extractor and being supplied from said second extractor to said first extractor without separation of lignin; (d) continuing said recirculation of said second used pulping liquor without separation of lignin to effect essentially isothermal initial extraction of said first charge at said predetermined pulping temperature and pressure, and thereafter withdrawing said second used pulping liquor from said first extractor; (e) flowing at least one additional used pulping liquor through said first charge in said first extractor on a once-through basis to effect essentially isothermal further extraction of said first charge at said predetermined pulping temperature and pressure, said additional used pulping liquor having a lower dissolved solids content than said second used pulping liquor and being obtained from step (f), as hereinafter described, during pulping of still another charge in a third extractor and being supplied from said third extractor to said first extractor without separation of lignin; (f) flowing heated fresh pulping liquor through said first charge in said first extractor on a once-through basis to effect essentially isothermal final extraction of said first charge; and (g) discharging crude cellulose pulp from said first extractor.

Claim 3

The process of claim 1 wherein said alcohol is selected from the group consisting of ethanol, methanol, and mixtures thereof, and the concentration of said alcohol is from about 20% to about 80% by weight.

Claim 4

The process of claim 2 wherein the concentration of said alcohol is from about 40% to about 60% by weight.

Claim 5

The process of claim 1 wherein said predetermined pulping temperature is from about 180° to about 210° C. and said predetermined pulping pressure is from about 20 to about 35 atmospheres.

Claim 6

The process of claim 1 wherein each of said extractors comprises an elongated vertical tubular vessel, the pulping liquors being passed upwardly through said vessel, and said vessel having a height:diameter ratio between about 4:1 and about 15:1.

Claim 7

The process of claim 1 further comprising the following steps between steps (f) and (g): draining liquor from said first extractor, depressurizing said first extractor by releasing the solvent vapors therein to a condenser, and recovering condensed solvent suitable for reuse as said fresh pulping liquor in step (f); and passing steam through said first extractor to strip residual solvent from said first charge, and condensing the stripped solvent vapors to obtain a condensate suitable for reuse as said fresh pulping liquor in step (f).

Claim 8

The process of claim 1 further comprising: steam stripping at least a portion of said second used pulping liquor withdrawn in step (d) at subatmospheric pressure, removing and condensing the stripped solvent vapors to obtain a condensate suitable for reuse as said fresh pulping liquor in step (f), and separating the resultant residual slurry containing lignin solids and dissolved carbohydrates.

Claim 9

The process of claim 1 further comprising the steps of: subjecting said second used pulping liquor withdrawn in step (d) at said predetermined pulping temperature and pressure to depressurization, and separating the resultant solvent vapors from residual used pulping liquor and being suitable for reuse as said first used pulping liquor in step (b); condensing said solvent vapors to obtain a condensate suitable for reuse as said fresh pulping liquor in step (f); and steam stripping at least a portion of said residual used pulping liquor at subatmospheric pressure, removing and condensing the stripped solvent vapors to obtain a condensate suitable for reuse as said fresh pulping liquor in step (f), and separating the resultant residual slurry containing lignin solids and dissolved carbohydrates.

Claim 10

In a solvent extraction pulping process wherein lignin is extracted from subdivided fibrous plant material by contacting said material at an elevated pulping temperature and pressure with a solvent pulping liquor comprising an aqueous solution of a lower aliphatic alcohol, the improvement which comprises providing a plurality of batch extractors and carrying out the following sequential steps in each extractor: (a) feeding a first charge of said subdivided fibrous plant material to a first extractor; (b) filling said first extractor with a first used pulping liquor so as to displace air from said first extractor; (c) introducing a second used pulping liquor of relatively high dissolved solids content at an elevated temperature and pressure into said first extractor so as to displace said first used pulping liquor, and recirculating said second used pulping liquor without separation of lignin at a relatively high velocity through said first extractor and through an external heat exchanger so as to effect rapid heating of said first charge to a predetermined pulping temperature of from about 160° to about 220° C. within not more than about 10 minutes at a predetermined pulping pressure of from about 10 to about 50 atmospheres, said second used pulping liquor being obtained from step (e), as hereinafter described, during pulping of another charge in a second extractor and being supplied from said second extractor to said first extractor without separation of lignin; (d) continuing said recirculation of said second used pulping liquor without separation of lignin to effect essentially isothermal initial extraction of said first charge at said predetermined pulping temperature and pressure, and thereafter withdrawing said second used pulping liquor from said first extractor; (e) flowing at least one additional used pulping liquor through said first charge in said first extractor on a once-through basis to effect essentially isothermal further extraction of said first charge at said predetermined pulping temperature and pressure, said additional used pulping liquor having a lower dissolved solids content than said second used pulping liquor and being obtained from step (f), as hereinafter described, during pulping of still another charge in a third extractor and being supplied from said third extractor to said first extractor without separation of lignin; (f) flowing heated fresh pulping liquor through said first charge in said first extractor on a once-through basis to effect essentially isothermal final extraction of said first charge, said fresh pulping liquor being obtained at least in part, from steps (g), (h), (k), and (l), as hereinafter described; (g) draining liquor from said first extractor, depressurizing said first extractor by releasing the solvent vapors therein to a condenser, and recovering condensed solvent suitable for reuse as said fresh pulping liquor in step (f); (h) passing steam through said first extractor to strip residual solvent from said first charge, and condensing the stripped solvent vapors to obtain a condensate suitable for reuse as said fresh pulping liquor in step (f); (i) discharging crude cellulose pulp from said first extractor; (j) subjecting said second used pulping liquor withdrawn in step (d) at said predetermined pulping temperature and pressure to depressurization, and separating the resultant solvent vapors from residual used pulping liquor; (k) condensing the solvent vapors from step (j) to obtain a condensate suitable for reuse as said fresh pulping liquor in step (f); and (l) steam stripping at least a portion of said residual used pulping liquor from step (j) at subatmospheric pressure, removing and condensing the stripped solvent vapors to obtain a condensate suitable for reuse as said fresh pulping liquor in step (f), and separating the resultant residual slurry containing lignin solids and dissolved carbohydrates.

Claim 11

In a solvent extraction pulping process wherein lignin is extracted from subdivided fibrous plant material by contacting said material at an elevated pulping temperature and pressure with a solvent pulping liquor comprising an aqueous solution of a lower aliphatic alcohol, the improvement which comprises providing a plurality of batch extractors and carrying out the following sequential steps in each extractor: (a) feeding a first charge of said subdivided fibrous plant material to a first extractor; (b) filling said first extractor with a first used pulping liquor so as to displace air from said first extractor; (c) introducing a second used pulping liquor of relatively high dissolved solids content at an elevated temperature and pressure into said first extractor so as to displace said first used pulping liquor, and recirculating said second used pulping liquor without separation of lignin at a relatively high velocity through said first extractor and through an external heat exchanger so as to effect rapid heating of said first charge to a predetermined pulping temperature of from about 160° to about 220° C. within not more than about 10 minutes at a predetermined pulping pressure of from about 10 to about 50 atmospheres, said second used pulping liquor being obtained from step (e), as hereinafter described, during pulping of another charge in a second extractor and being supplied from said second extractor to said first extractor without separation of lignin; (d) continuing said recirculation of said second used pulping liquor without separation of lignin to effect essentially isothermal initial extraction of said first charge at said predetermined pulping temperature and pressure, and thereafter withdrawing said second used pulping liquor from said first extractor; (e) flowing at least one additional used pulping liquor through said first charge in said first extractor on a once-through basis to effect essentially isothermal further extraction of said first charge at said predetermined pulping temperature and pressure, said additional used pulping liquor having a lower dissolved solids content than said second used pulping liquor and being obtained from step (f), as hereinafter described, during pulping of still another charge in a third extractor and being supplied from said third extractor to said first extractor without separation of lignin; (f) flowing heated fresh pulping liquor through said first charge in said first extractor on a once-through basis to effect essentially isothermal final extraction of said first charge, said fresh pulping liquor being obtained at least in part, from steps (g), (h), (k), and (l), as hereinafter described; (g) draining liquor from said first extractor, depressurizing said first extractor by releasing the solvent vapors therein to a condenser, and recovering condensed solvent suitable for reuse as said fresh pulping liquor in step (f); (h) passing steam through said first extractor to strip residual solvent from said first charge, and condensing the stripped solvent vapors to obtain a condensate suitable for reuse as said fresh pulping liquor in step (f); (i) discharging crude cellulose pulp from said first extractor; (j) subjecting said second used pulping liquor withdrawn in step (d) at said predetermined pulping temperature and pressure to depressurization, and separating the resultant solvent vapors from residual used pulping liquor; (k) condensing the solvent vapors from step (j) to obtain a condensate suitable for reuse as said fresh pulping liquor in step (f); and (l) steam stripping at least a portion of said residual used pulping liquor from step (j) at subatmospheric pressure, removing and condensing the stripped solvent vapors to obtain a condensate suitable for reuse as said fresh pulping liquor in step (f), and separating the resultant residual slurry containing lignin solids and dissolved carbohydrates.

Claim 12

The process of claim 9 wherein said alcohol is selected from the group consisting of methanol, ethanol, the propanols, and the butanols, and the concentration of said alcohol is from about 20% to about 80% by weight.

Claim 13

The process of claim 10 wherein the concentration of said alcohol is from about 40% to about 60% by weight.

Claim 14

The process of claim 9 wherein said predetermined pulping temperature is from about 180° to about 210° C. and said predetermined pulping pressure is from about 20 to about 35 atmospheres. 13. The process of claim 9 wherein each of said extractors comprises an elongated vertical tubular vessel, the pulping liquors being passed upwardly through said vessel, and said vessel having a height:diameter ratio between about

Claim 15

4:1 and about 15:1. 14. The process of claim 9 further comprising the steps of settling the residual slurry from step (1) to obtain a thickened lignin slurry and a supernatant liquor, centrifuging said thickened slurry to separate a lignin sludge from another supernatant liquor, combining said supernatant liquors, and concentrating the combined liquors by

Claim 16

evaporation to obtain a carbohydrate concentrate. 15. The process of claim 14 wherein the solvent vapors from step (j) are condensed to provide heat

Claim 17

for the evaporation. 16. The process of claim 9 wherein said residual used pulping liquor from step (j) is at a relatively low temperature and is supplied to step (b) as said first pulping liquor.