Processes for producing high-yield pulp and paper products
An improved semichemical pulping process is disclosed to reduce washing costs and recovery process costs, while producing equivalent pulp and paper products. In some variations, the invention provides a process for producing a paper product from biomass, comprising: digesting lignocellulosic biomass in the presence of steam and/or hot water to generate an intermediate pulp material and a liquid phase containing extracted hemicelluloses; mechanically refining the intermediate pulp material, to generate a refined pulp material; and introducing the refined pulp material, the liquid phase, and optionally a separate solid material to a paper machine, to produce a paper product. The process optionally employs no washing step. When the liquid phase is washed from the intermediate pulp material or the refined pulp material using an aqueous wash solution, the wash filtrate may be introduced directly or indirectly to the paper machine.
1. A process for producing a paper product from biomass, said process comprising:
(a) providing lignocellulosic biomass comprising cellulose, hemicellulose, and lignin;
(b) digesting said biomass in the presence of steam and/or hot water to generate an intermediate pulp material and a liquid phase, wherein said liquid phase contains extracted hemicelluloses and lignin;
(c) evaporating said liquid phase to remove volatile components, thereby generating a solids-enriched liquid phase;
(d) mechanically refining said intermediate pulp material, to generate a refined pulp material; and
(e) introducing said refined pulp material, said solids-enriched liquid phase, and optionally a separate solid material to a paper machine, to produce a paper product,
wherein said process further comprises washing said liquid phase from said intermediate pulp material using an aqueous wash solution, to generate an intermediate pulp material wash filtrate, and evaporating said intermediate pulp material wash filtrate to remove volatile components, thereby generating a solids-enriched intermediate pulp material wash filtrate; wherein said solids-enriched intermediate pulp material wash filtrate is introduced to said paper machine.
2. The process of claim 1 , wherein step (b) is conducted using said steam in saturated, superheated, or supersaturated form.
3. The process of claim 1 , wherein step (b) is conducted using hot water.
4. The process of claim 1 , wherein step (b) is conducted at a digestor temperature selected from about 140° C. to about 220° C.
5. The process of claim 1 , wherein step (b) is conducted at a digestor residence time selected from about 1 minute to about 60 minutes.
6. The process of claim 1 , wherein said refined pulp material is not separately washed.
7. A process for producing a paper product from biomass, said process comprising:
(a) providing lignocellulosic biomass comprising cellulose, hemicellulose, and lignin;
(b) digesting said biomass in the presence of steam and/or hot water to generate an intermediate pulp material and a liquid phase, wherein said liquid phase contains extracted hemicelluloses and lignin;
(c) evaporating said liquid phase to remove volatile components, thereby generating a solids-enriched liquid phase;
(d) mechanically refining said intermediate pulp material, to generate a refined pulp material; and
(e) introducing said refined pulp material, said solids-enriched liquid phase, and optionally a separate solid material to a paper machine, to produce a paper product,
wherein said process further comprises washing said liquid phase from said refined pulp material using an aqueous wash solution, to generate a refined pulp material wash filtrate, and evaporating said refined pulp material wash filtrate to remove volatile components, thereby generating a solids-enriched refined pulp material wash filtrate;
wherein said solids-enriched refined pulp material wash filtrate is introduced to said paper machine.
8. The process of claim 7 , wherein step (b) is conducted using said steam in saturated, superheated, or supersaturated form.
9. The process of claim 7 , wherein step (b) is conducted using hot water.
10. The process of claim 7 , wherein step (b) is conducted at a digestor temperature selected from about 140° C. to about 220° C.
11. The process of claim 7 , wherein step (b) is conducted at a digestor residence time selected from about 1 minute to about 60 minutes.
12. The process of claim 7 , wherein said intermediate pulp material is not separately washed.