초록

A process for the recovery of organic chemical feedstocks from biooil is presented. The process comprises separating the water soluble chemicals from biomass and recovering the primarily oxygenate compounds for use as feedstocks.

대표청구항 ▼

1. A process for obtaining chemical precursors from biooil, the process comprising the steps of: lightly hydrotreating the biooil, wherein the lightly hydrotreating conditions comprises a temperature between 300° C. and 400° C., under a hydrogen partial between preferably between 670 kPa and 13.8 MP

1. A process for obtaining chemical precursors from biooil, the process comprising the steps of: lightly hydrotreating the biooil, wherein the lightly hydrotreating conditions comprises a temperature between 300° C. and 400° C., under a hydrogen partial between preferably between 670 kPa and 13.8 MPa, and at space velocities (WHSV) from 0.1 hr−1 to 5.0 hr−l;separating the biooil after the step of lightly hydrotreating into a first stream comprising a water-soluble phase and a second stream comprising pyrolytic lignin;lightly hydrotreating the pyrolytic lignin phase to increase the yields of oxygenated compounds;concentrating the water-soluble phase by removing water thereby creating a concentrated organic phase of organic compounds comprising ketones, alcohols, phenols, carboxylic acids, carbohydrates, and mixtures thereof; and passing the concentrated organic phase to a catalytic reactor to upgrade the organic compounds. 2. The process of claim 1 further comprising the step of separating the concentrated organic phase into a plurality of concentrated streams comprising a first concentrated stream comprising aldehydes, a second concentrated stream comprising organic acids, a third concentrated stream comprising ketones, a fourth concentrated stream comprising phenols, and a fifth concentrated stream comprising non-aromatic alcohols, and wherein the step of passing comprises passing at least one of the plurality of concentrated streams to the catalytic reactor. 3. The process of claim 1 wherein the step of separating comprises using a gravimetric filtration process to separate the biooil. 4. The process of claim 1 wherein the step of separating comprises adding water to the biooil to create an aqueous phase. 5. The process of claim 1 wherein the step of concentrating the water-soluble phase comprises removing water from the water-soluble phase using a separation process selected from the group consisting of evaporation, distillation, extraction, membrane separation, adsorption separation, and combinations thereof. 6. The process of claim 1 further comprising the step of pretreating the biooil prior to the step of lightly hydrotreating to remove alkali and alkaline earth metals and to form a pretreated biooil, and wherein the step of lightly hydrotreating comprises contacting the pretreated biooil with a hydrotreating catalyst and the step of separating the biooil comprises separating the pretreated biooil into the first stream and the second stream. 7. The process of claim 1 wherein the step of lightly hydrotreating comprises contacting the biooil with a hydrotreating catalyst that is stable to alkali and alkaline earth metals. 8. A process for obtaining chemical precursors from biooil, the process comprising the steps of: lightly hydrotreating the biooil, wherein the lightly hydrotreating conditions comprises a temperature between 300° C. and 400° C., under a hydrogen partial between preferably between 670 kPa and 13.8 MPa, and at space velocities (WHSV) from 0.1 hr−1 to 5.0 hr−1;separating the biooil into a first stream comprising a water-soluble phase and a second stream comprising pyrolytic lignin;pretreating the water-soluble phase to remove alkali and alkaline earth metals;concentrating the water-soluble phase after the step of pretreating by removing water thereby creating a concentrated organic phase of organic compounds comprising ketones, alcohols, phenols, carboxylic acids, carbohydrates, and mixtures thereof; andpassing the concentrated organic phase to a catalytic reactor to upgrade the organic compounds. 9. A process for obtaining chemical precursors from pyrolysis oil formed from pyrolyzing biomass, the process comprising the steps of: partially deoxygenating the pyrolysis oil comprising biooil to produce an intermediate stream comprising aromatic compounds, oxygenates and water, the biooil comprising water, pyrolytic lignin, aldehydes, carboxylic acids, carbohydrates, phenols, furfurals, alcohols, ketones, and mixtures thereof, wherein the partial deoxygenation of the pyrolysis oil comprising hydrotreating the pyrolysis oil in a hydrotreating unit, under hydrotreating conditions comprising a temperature between 300° C. and 400° C., under a hydrogen partial between preferably between 670 kPa and 13.8 MPa, and at space velocities (WHSV) from 0.1 hr−1 to 5.0 hr−1 ;separating the intermediate stream into a first stream comprising a water-soluble phase that comprises organic compounds including oxygenates and a second stream comprising aromatic compounds;concentrating the first stream by removing water, thereby creating a concentrated organic phase; andpassing the concentrated organic phase to a catalytic reactor to upgrade the organic compounds. 10. The process of claim 9 further comprising the step of adding chemical agents to the pyrolysis oil for solubilizing and dispersing solids in the pyrolysis oil prior to the step of partially deoxygenating. 11. The process of claim 9 wherein the step of separating comprises using a gravimetric filtration process to separate the intermediate stream. 12. The process of claim 9 wherein the step of separating comprises adding water to the pyrolysis oil to create an aqueous phase. 13. The process of claim 9 wherein the step of concentrating the water-soluble phase comprises using a separation process selected from the group consisting of evaporation, distillation, extraction, membrane separation, adsorption separation, and combinations thereof. 14. The process of claim 8 further comprising the step of separating the concentrated organic phase into a plurality of concentrated streams comprising at least a concentrated first stream comprising aldehydes, a second concentrated stream comprising organic acids, a third concentrated stream comprising ketones, a fourth concentrated stream comprising phenols, and a fifth concentrated stream comprising non-aromatic alcohols, and wherein the step of passing comprises passing the plurality of concentrated streams to the catalytic reactor. 15. The process of claim 8 wherein the step of separating comprises adding water to the biooil to create an aqueous phase. 16. The process of claim 8 wherein the step of concentrating the water-soluble phase comprises removing water from the water-soluble phase using a separation process selected from the group consisting of evaporation, distillation, extraction, membrane separation, adsorption separation, and combinations thereof.