Integrated process for the pre-treatment of biomass and production of bio-oil

1. An integrated process for the conversion of a biomass with an impurity content, the process comprising pretreating the biomass to convert the biomass into a quality feedstock with a desired moisture content; and transporting the pretreated and converted biomass for the production of biochemicals and biofuels;

wherein said pretreating is a leaching process comprising the following phases:

a1. feeding at least one biomass or mixture of biomasses to a tank with a stirring system;

a2. recovering an untreated effluent from an existing and adjacent factory, plant or mill, and wherein the untreated effluent is defined from the group consisting of effluents from a cellulose production mill, effluents from the sugarcane or energy cane processing plant, or effluents from the cellulose sugar production plant

b. adding the untreated effluent of phase (a2) as a solvent to the biomass of phase (a1) to form a solid/solvent mixture;

c. adjusting the consistency of the solid/solvent mixture;

d. stirring the solid/solvent mixture;

e. discharging material obtained in phase (d) for separation of liquid and solid phases;

f. sending the liquid phase to a biomass fines recovery system;

g. feeding the solid material to a secondary dewatering system to obtain a high quality pretreated biomass;

wherein the biomass of step (b) is a plant biomass defined from the group consisting of: wood, including bark and chips, leaves and roots; shrub and herbaceous biomass, including grasses and weeds; sugarcane, including bagasse resulting from the processing in the industry and straw from the harvest; energy cane as a whole, or just stems; straw and agricultural residues from the processing of maize, including the cob and leaves; cereal straw such as rice, wheat, rye, inter alia, and sawdust, cardboard and urban organic waste; or a mixture thereof,

wherein the leaching time is between 1 and 5 minutes,

wherein the moisture range of the pretreated biomass is between 56% and 80%,

wherein the pretreated biomass has a potassium content between 209 and 1200 ppm, and

wherein the pretreated biomass has a sodium content between 200 and 650 ppm.

2. Process, in accordance with claim 1 , wherein the wood is selected from a group consisting of araucaria ; long fiber cedar wood; cypress; Rocky Mountain Douglas fir; European yew; hemlock; kauri; kaya; larch; pine tree; redwood; rimu; fir; sugi; acacia; azalea; albizia (lebbek tree); alder; apple tree; arbutus; ash wood; aspen; Australian red cedar; ayan; balsa tree; linden; beech; birch; sweet-chestnut; ebony; bocote; maple; boxwood; Brazilwood; bubinga; horse-chestnut; white walnut; catalpa; cherry tree; carap; red chestnut; Ceratopelatum apetalum (coachwood); cocobolo; willow tree; Canadian poplar; magnolia ; Cornelian cherry; ebony; elm; eucalyptus ; cogwood; passiflora ; Tupelo; pecan; hardwood tree; juca; ipe tree; iroko; casuarina; jacaranda; courbaril; sycamore; laurel; terminalia; Lignum vitae ; carob tree; mahogany; maple; meranti; mpingo; oak; obeche; okoumé; Oregon myrtle; California bay laurel tree; pear tree; poplar; ramin; red-cedar; Brazilian rosewood tree; shala tree; sandal wood; sassafras ; Indian satinwood; silky oak; silver wattle; snakeroot; azedeira; Spanish cedar; American sycamore; teak, walnut; willow tree; tulip tree; bamboo; palm tree; and combinations/hybrids thereof.

3. Process, in accordance with claim 2 , wherein the wood is eucalyptus.

4. Process, in accordance with claim 1 , wherein the biomass is energy cane.

5. Process, in accordance with claim 1 , wherein the biomass consists of wood chips, wood bark, or a combination thereof.

6. Process, in accordance with claim 5 , wherein the biomass consists of wood bark in a quantity between 5% and 100%.

7. Process, in accordance with claim 6 , wherein the biomass consists of wood bark in a quantity between 30% and 100%.

8. Process, in accordance with claim 1 , wherein the adjustment of the consistency of the mixture in phase (c) is carried out by adding solvent until said consistency is between 1 and 30% of solid content on a mass basis.

9. Process, in accordance with claim 8 , wherein the solvent is added until the consistency is between 2% and 15% of solid content on a mass basis, or between 5% and 15% of solid content on a mass basis.

10. Process, in accordance with claim 1 , wherein phase (d) occurs in a medium having a temperature between 25° C. and 100° C.

11. Process, in accordance with claim 1 , wherein phase (d) occurs in a medium having a pH between 2.0 and 11.0.

12. Process, in accordance with claim 1 , wherein the stirring in phase (d) varies between 5 and 1000 rpm.

13. Process, in accordance with claim 1 , wherein the moisture range of the pretreated biomass is between 56% and 70%.

14. Process, in accordance with claim 1 , wherein the pretreated biomass has a chlorine content up to 100 ppm.

15. Process, in accordance with claim 1 , wherein the ash content of the biomass is reduced.