US2012198758A1PendingUtilityA1
Hydrothermal Processing (HTP) of Algae Grown in HTP Waste Streams
Est. expiryOct 22, 2029(~3.3 yrs left)· nominal 20-yr term from priority
C12N 1/12Y02W10/37C12P 7/6463
50
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Claims
Abstract
A process for the conversion of organic waste to biofuel is provided comprising cultivating organisms in the aqueous product of the HTP conversion process.
Claims
exact text as granted — not AI-modified1 . A process for conversion of organic biowaste to biocrude oil comprising:
providing a concentrated biosolid fraction and a bypass liquid fraction obtained from organic biowaste; subjecting the concentrated biosolid fraction to a hydrothermal process under conditions sufficient to obtain a biocrude oil product, an aqueous residual product, and a gaseous residual product; cultivating an organism in a culturing media to obtain a cultivated mixture; recovering a concentrated cultivated organism fraction from the cultivated mixture; and introducing the concentrated cultivated organism fraction and optionally the concentrated biosolid fraction to the hydrothermal process.
2 . The process of claim 1 , wherein the culturing media comprises the aqueous residual product.
3 . The process of claim 2 , wherein the culturing media further comprises the bypass liquid fraction.
4 . The process of claim 3 , wherein at least 50% of the culturing media by volume is bypass liquid fraction.
5 . The process of claim 1 , further comprising separating a concentrated biosolid fraction and a bypass liquid fraction from organic biowaste.
6 . The process of claim 3 , further comprising separating a concentrated biosolid fraction and a bypass liquid fraction from organic biowaste.
7 . The process of claim 5 , wherein the bypass liquid fraction is at least 50 percent of the organic biowaste on a total volume basis.
8 . The process of claim 5 , wherein the bypass liquid fraction is at least 80 percent of the organic biowaste on a total volume basis.
9 . The process of claim 1 , wherein the concentrated biosolid fraction comprises at least 5 percent total solids by weight.
10 . The process of claim 1 , wherein the concentrated biosolid fraction comprises at least 10 percent total solids by weight.
11 . The process of claim 1 , wherein the concentrated cultivated organism fraction comprises at least 5 percent by weight total solids.
12 . The process of claim 1 , wherein the concentrated cultivated organism fraction comprises at least 10 percent by weight total solids.
13 . The process of claim 1 , wherein the ratio of concentrated cultivated organism fraction to concentrated biosolid fraction introduced to the hydrothermal process is greater than about 5 percent on a total solids basis.
14 . The process of claim 6 , wherein the ratio of concentrated cultivated organism fraction to concentrated biosolid fraction introduced to the hydrothermal process is greater than about 5 percent on a total solids basis.
15 . The process of claim 1 , wherein the ratio of concentrated cultivated organism fraction to concentrated biosolid fraction introduced to the hydrothermal process is greater than about 25 percent on a total solids basis.
16 . The process of claim 6 , wherein the ratio of concentrated cultivated organism fraction to concentrated biosolid fraction introduced to the hydrothermal process is greater than about 25 percent on a total solids basis.
17 . The process of claim 1 , further comprising introducing the gaseous residual product to the culturing media.
18 . The process of claim 6 , further comprising introducing the gaseous residual product to the culturing media.
19 . (canceled)
20 . The process of claim 1 , wherein the organic biowaste is animal waste.
21 . (canceled)
22 . The process of claim 1 , wherein the organic biowaste is human waste from a municipal sewage stream.
23 . (canceled)
24 . The process of claim 1 , wherein the organism is algae or bacteria.
25 . (canceled)
26 . (canceled)
27 . The process of claim 1 , wherein the organism is Chlorella or Spirulina.
28 . The process of claim 1 , wherein the algae comprises less than 20 weight percent lipid.
29 . The process of claim 1 , wherein the hydrothermal process is carried out at a temperature less than 320° C. and at a pressure above 0.5 MPa.
30 . The process of claim 1 , wherein the biocrude oil product is characterized by a heating value of at least 25,000 kJ/kg.
31 . The process of claim 1 , wherein the concentrated cultivated organism fraction comprises algae and bacteria.
32 . (canceled)
33 . A process for conversion of organic biowaste to biocrude oil comprising:
separating a concentrated biosolid fraction and a bypass liquid fraction obtained from organic biowaste; wherein the organic waste is selected from the group consisting of animal waste, human waste and food processing waste; introducing the concentrated biosolid fraction to a hydrothermal process under conditions sufficient to obtain a biocrude oil product, an aqueous residual product, and a gaseous residual product; wherein the hydrothermal process is carried out at a temperature less than 320° C. and at a pressure above 0.5 MPa; cultivating an organism comprising algae in a culturing media comprising the aqueous product and the bypass liquid fraction to obtain a cultivated mixture; recovering a concentrated cultivated organism fraction from the cultivated mixture; introducing the concentrated cultivated organism fraction to the hydrothermal process; wherein the ratio of concentrated cultivated organism fraction to concentrated biosolid fraction introduced to the hydrothermal process is greater than about 25 percent on a total solids basis.Join the waitlist — get patent alerts
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