Metal impurity and high molecular weight components removal of biomass derived biocrude

1. A process comprising the steps of:

a) providing a biocrude derived from biomass, wherein the biomass comprises at least one metal impurity and at least one high molecular weight component;

b) admixing said biocrude with a first solvent and a second solvent to form a mixture, wherein said first solvent comprises at least one of methanol, ethanol, propanol or acetone, wherein said second solvent comprises at least one of methyl ether, diethyl ether, dipropyl ether, tetrahydrofuran, tetrahydrofurfuryl alcohol, or methyl tert-butyl ether;

c) subjecting said mixture to a separation device to form a liquid phase and a solid phase, wherein said liquid phase comprises less than 20% (by weight) of components having a molecular weight greater than 937 Daltons; and

d) recovering said liquid phase.

2. The process of claim 1 , wherein said liquid phase comprises less than 50% of the total metal impurity from said biocrude in step (a), and wherein said liquid phase comprises less than 15% of any high molecular weight components from said biocrude in step (a).

3. The process of claim 1 , wherein said biomass derived biocrude comprises sugar monomer, wherein said sugar monomer comprises at least one sugar alcohol, one sugar, or any combination thereof.

4. The process of claim 1 , wherein said biomass derived biocrude comprises at least one of tars, pyrolysis oil, pyrolytic lignin, acids, chars, alcohols, aldehydes, esters, ketone, aromatics, or any combination thereof.

5. The process one of claim 1 , wherein said high molecular weight component has a molecular weight of at least 937 Daltons.

6. The process of claim 1 , wherein said metal impurity comprises at least one of Na, K, Ca, Mg, Fe, Al, Si, Mn and P.

7. The process of claim 1 , wherein said high molecular component comprises at least one of organic oligomers, polymers or combination thereof, and wherein said organic oligomers or said polymers are derived from at least one of carbohydrate, lignin components, or combination thereof, in the biomass.

8. The process of claim 1 , wherein said second solvent comprises at least one of methyl ether, diethyl ether, dipropyl ether, tetrahydrofuran, tetrahydrofurfuryl alcohol, or any combination thereof.

9. The process of claim 1 , wherein said biomass derived biocrude is pyrolysis oil, wherein said pyrolysis oil is mixed with said first solvent and said second solvent in a weight ratio of between one and ten parts pyrolysis oil to one part of said first solvent also to between one and 20 parts of said second solvent.

10. The process of claim 1 ,

wherein said biomass derived biocrude is corn fiber-based pyrolysis oil,

wherein said first solvent is methanol,

wherein said second solvent is methyl-t-butyl ether (MTBE),

wherein said corn fiber-based pyrolysis oil is mixed with said methanol and said MTBE in the weight ratio of 1:1:1,

wherein said liquid phase comprises less than 37% of the amount of said metal impurity compare to which is in said biomass derived biocrude in said step (a), and

wherein said liquid phase comprises less than 15% of the amount of said high molecular weight component compare to which is in said biomass derived biocrude in step (a).

11. The process of claim 1 ,

wherein said biomass derived biocrude is wood-based pyrolysis oil,

wherein said first solvent is methanol,

wherein said second solvent is methyl-t-butyl ether (MTBE),

wherein said wood-based pyrolysis oil is mixed with said methanol and said MTBE in the weight ratio of 3:1:10,

wherein said liquid phase has a decreased amount of said high molecular weight components compare to which is in said wood-based pyrolysis oil.

12. The process of claim 11 ,

wherein said wood-based pyrolysis oil comprises components having a molecular weight range from 360 to 6359 Daltons, and

wherein said liquid phase contains less than 20% (by weight) of components with molecular weight greater than 937 Daltons.

13. The process of claim 1 ,

wherein said wood-based pyrolysis oil comprises at least 62% of components with molecular weight of greater than 937 Dalton, and

wherein said liquid phase comprises less than 20% of components with molecular weight of greater than 937 Dalton.

14. The process of claim 1 , further including the step of reacting said liquid phase with a catalyst under a condition sufficient to produce a reaction product containing fuel range hydrocarbon.

15. The process of claim 14 ,

wherein said catalyst is hydrotreating catalyst comprises at least one of molybdenum, cobalt, nickel and tungsten;

wherein said condition includes a pressure range of from about 100 to about 2000 psig and a temperature in the range of from about 260° C. to about 430° C.; and

wherein said fuel range hydrocarbon is a gasoline or a diesel boiling range hydrocarbon.

16. The process of claim 14 ,

wherein said catalyst is hydrotreating catalyst comprising molybdenum and nickel;

wherein said condition includes a pressure range of from about 100 to 2000 psig and a temperature in the range of from about 260° C. to about 430° C.; and

wherein said fuel range hydrocarbon is a diesel boiling range hydrocarbon.

17. The process of claim 14 ,

wherein said catalyst comprises zeolite,

wherein said condition includes a pressure range of from about 1 to about 500 psig and a temperature in the range of from about 200° C. to about 800° C.; and

wherein said fuel range hydrocarbon is gasoline boiling range hydrocarbon.

18. The process of claim 1 , wherein said zeolite is selected from the group consisting of ZSM-5, ZSM-8, ZSM-11, ZSM-12, ZSM-35, ZSM-38 and combinations thereof.

19. The process of claim 1 further including the step of pyrolyzing a biomass to produce said biocrude provided in step (a).