Methods and apparatuses for forming low-metal biomass-derived pyrolysis oil
Methods and apparatuses for forming a low-metal biomass-derived pyrolysis oil are provided. In an embodiment, a method for forming a low-metal biomass-derived pyrolysis oil includes washing biomass comprising a water-soluble metal component therein with wash water that is substantially free of water-soluble metals. The washed biomass and water containing water-soluble metal are separated after washing the biomass. The washed biomass is pyrolyzed in a pyrolysis process to form a pyrolysis vapor stream. A portion of the pyrolysis vapor stream is condensed to form a condensate. The wash water is derived from the washed biomass. In an embodiment of an apparatus, the apparatus comprises a washing stage, a biomass dryer, a pyrolysis reactor, a quenching system comprising a primary condenser and a secondary condenser, and a return line that connects the quenching system to the washing stage.
1. A method for forming a biomass-derived pyrolysis oil, the method comprising the steps of:
washing biomass comprising a water-soluble metal component therein with wash water;
separating the washed biomass and water containing water-soluble metal after washing the biomass, the washed biomass having a reduced level of metals compared to the biomass before washing;
pyrolyzing the washed biomass in a pyrolysis process to form a pyrolysis vapor stream; and
condensing a portion of the pyrolysis vapor stream to form a condensate having a reduced level of metals compared to the biomass before washing;
wherein at least a portion of the wash water comprises a portion of the condensate.
2. The method of claim 1 , wherein the step of condensing comprises forming a water-rich condensate having a water concentration of at least 30 weight %, based upon the total weight of the water-rich condensate.
3. The method of claim 2 , wherein the water-rich condensate comprises a water-rich phase and an oil-rich phase, and wherein the water-rich phase is separated from the oil-rich phase.
4. The method of claim 3 , wherein the separated water-rich phase comprises the wash water.
5. The method of claim 4 , wherein the separated water-rich phase is purified prior to washing the biomass with the wash water.
6. The method of claim 2 , wherein the step of condensing comprises a primary condensing stage at a temperature of from about 40 to about 70° C. to yield a primary condensate.
7. The method of claim 6 , wherein the step of condensing further comprises a secondary condensing stage at a temperature of from about 30 to about 50° C., and wherein the secondary condensing stage yields the water-rich condensate separate from the primary condensate.
8. The method of claim 1 , further comprising digesting the bioass, wherein the step of washing the biomass comprises mixing the wash water and biomass during digestion.
9. The method of claim 1 , further comprising:
digesting the biomass, the digested biomass comprising fiber and optionally nuts; and
optionally removing the nuts from the fiber:
wherein the step of washing the biomass occurs after digestion and the optional nut removal step.
10. The method of claim 1 , wherein the step of separating the washed biomass and water further comprises drying the washed biomass prior to pyrolyzing to a water content of from about 6 to about 10 weight %, based on the total weight of the washed biomass after drying.
11. A method for forming a biomass-derived pyrolysis oil, the method comprising the steps of:
washing lignocellulosic biomass with wash water, the lignocellulosic biomass having a water-soluble metal component present in an amount of at least about 0.7 weight % based on the total raw weight of the biomass;
separating the washed lignocellulosic biomass and water containing water-soluble metal after washing the biomass;
pyrolyzing the washed lignocellulosic biomass in a pyrolysis process to form a pyrolysis vapor stream; and
condensing a portion of the pyrolysis vapor stream in a quenching system comprising a primary condenser and a secondary condenser wherein the secondary condenser yields a water-rich condensate having a water concentration of at least 30 weight %, based upon the total weight of the water-rich condensate;
wherein at least a portion of the wash water comprises a portion of the water-rich condensate of the pyrolysis vapor stream.
12. The method of claim 11 , wherein the primary condenser and the secondary condenser each comprise a direct-contact condenser column and a condensate recirculation system.
13. The method of claim 11 , wherein the water-rich condensate comprises a water-rich phase and an oil-rich phase, and wherein the water-rich phase is separated from the oil-rich phase.
14. The method of claim 13 , wherein the separated water-rich phase comprises the wash water.
15. The method of claim 14 , wherein the separated water-rich phase is purified prior to washing the biomass with the wash water.
16. The method of claim 11 , wherein the primary condenser is operated at a temperature of from about 40 to about 70° C. and the secondary condenser is operated at a temperature of from about 30 to about 50° C.
17. The method of claim 11 , further comprising digesting the biomass, wherein the step of washing the biomass comprises mixing the wash water and biomass during digestion.
18. The method of claim 11 , further comprising:
digesting the biomass, the digested comprising fiber and optionally nuts; and
optionally removing the nuts from the fiber:
wherein the step of washing the biomass occurs after digestion and the optional nut removal step.
19. The method of claim 1 wherein the wash water has less than or equal to 500 ppm water-soluble metals.
20. The method of claim 11 wherein the wash water has less than or equal to 500 ppm water-soluble metals.
21. The method of claim 10 wherein the wash water further comprises an acid.