Bio-oil fractions composition derived from bio-oil
US-2024381867-A1 · Nov 21, 2024 · US
US9822309B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9822309-B2 |
| Application number | US-201113038134-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 1, 2011 |
| Priority date | Feb 5, 2002 |
| Publication date | Nov 21, 2017 |
| Grant date | Nov 21, 2017 |
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Provided is a process where the biomass and bisolids are hydrothermally treated under a reductive gas. Using this process a high carbon content pumpable mixture of biomass and biosolid slurry is produced with a viscosity value of less than 1.5.
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The invention claimed is: 1. A process for producing a pumpable high carbon content slurry comprising: providing a mixture of water and a material selected from the group consisting of an agricultural product, wood, plant, paper and cardboard, wherein the material comprises a weight percentage between 30 wt % to 70 wt % of the mixture; mixing the mixture with a residue produced from a waste water treatment process to form a slurry mixture; and heating the slurry mixture under a non-oxidative gas to thereby produce the high carbon content slurry. 2. The process of claim 1 , wherein the non-oxidative gas is selected from the group consisting of argon, helium, nitrogen, hydrogen, carbon dioxide, or gaseous hydrocarbons, or mixtures thereof. 3. The process of claim 1 in which the slurry mixture is heated to the temperature having a range of 170 to 250° C. 4. The process of claim 1 , wherein the slurry mixture is heated under the non-oxidative gas at a pressure of 100 to 400 psi. 5. A process for converting biomass into a higher carbon content slurry, consisting essentially of: grinding the biomass; mixing the biomass with water to thereby form a first mixture, wherein the biomass comprises a weight percentage between 30 wt % to 70 wt % of the first mixture; mixing the first mixture with a residue produced from a waste water treatment process to form a slurry mixture; and heating the slurry mixture under a non-oxidative gas to thereby produce the high carbon content slurry. 6. The process of claim 5 , wherein the biomass is selected from the group consisting of an agricultural product, wood, plant, paper and cardboard. 7. The process of claim 5 , wherein the non-oxidative gas is selected from the group consisting of argon, helium, nitrogen, hydrogen, carbon dioxide, or gaseous hydrocarbons, or mixtures thereof. 8. The process of claim 5 , the slurry mixture is heated under the non-oxidative gas at a pressure of 100 to 400 psi.
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