Method for producing ethanol from biomass

• US 4,952,504 A
• Filed: 07/28/1987
• Issued: 08/28/1990
• Est. Priority Date: 07/28/1987
• Status: Expired due to Fees

• Current Assignee: Stanley J. Pavilon
• Original Assignee: Stanley J. Pavilon
• Inventors: Pavilon, Stanley J.
• Primary Examiner(s): Warden, Robert J.
• Assistant Examiner(s): McMahon, Timothy M.
• Application Number:
  US07/079,138
• Time in Patent Office: 1,127 Days
• Field of Search: 435/163, 435/164, 435/165, 426/49, 426/52-53, 426/54, 426/616, 426/635, 426/807
• US Class Current: 435/163
• CPC Class Codes: C12P 7/06 Ethanol, i.e. non-beverage
• CPC Class Codes: C12P 7/08 produced as by-product or from waste or cellulosic material substrate
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel
• CPC Class Codes: Y10S 426/807 Poultry or ruminant feed

Abstract

Biomass slurry is hydrolyzed in a fuel fired hydrolysis heater. When the biomass is fruit waste, the organic acid in the waste is used as the hydrolysis catalyst. When the biomass does not contain organic acid, carbon dioxide generated in a fermenter is fed to the hydrolysis heater as carbonic acid to provide the catalyst. Solids are separated from the hydrolyzed effluent, and flue gas from the hydrolysis heater is used to dry same. The effluent is fermented and subsequently distilled at substantially atmospheric pressure to produce ethyl alcohol vapor. The vapor is fed to a vacuum distillation tower for producing anhydrous ethyl alcohol. Vacuum distillation tower bottoms provide the reflux for the atmospheric distillation unit. A portion of the stillage from the atmospheric distillation unit is recycled by mixing with new feedstock. The remaining stillage is evaporated to a syrup, mixed with unreacted solids, and dried to produce an animal feed byproduct.

Claims

1. A method of producing ethanol from biomass comprising the steps of providing biomass containing organic acid, mixing said biomass with water to form a biomass slurry, hydrolyzing said slurry in fuel fired hydrolysis means, utilizing said organic acid for catalyzing hydrolysis of said slurry, separating said slurry into liquid and solids after said hydrolyzing step, utilizing flue gas from said fuel fired hydrolysis means for drying said solids, and further processing said liquid to produce ethanol.

2. A method of producing ethanol from biomass comprising the steps of providing biomass containing organic acid, mixing said biomass with water to form a biomass slurry, hydrolyzing said slurry at a temperature and pressure for catalyzing hydrolysis of said slurry with said organic acid that is contained in said biomass, and further processing effluent from said step of hydrolyzing to produce ethanol.

3. The method of claim 2 including the step of fermenting at least part of the effluent from said hydrolyzing step to generate carbon dioxide, selectively utilizing at least part of said carbon dioxide in the form of carbonic acid for supplementing catalysis of said slurry during said hydrolyzing step, and said step of further processing effluent to produce ethanol being carried out subsequent to said fermenting step on effluent sued for said fermenting step.

4. A method of producing ethanol from biomass comprising the steps of providing biomass containing organic acid that is naturally present in the biomass, mixing said biomass with water to form a biomass slurry, hydrolyzing said slurry at a temperature and pressure for catalyzing hydrolysis of said slurry with said organic acid that is naturally present in the biomass without the addition of any additional acid, and further processing effluent from said step of hydrolyzing to produce ethanol.

5. The method of claim 4 wherein said step of providing biomass is carried out by providing biomass that is primarily citrus residue.

6. The method of claim 4 wherein said hydrolyzing step is carried out by hydrolyzing said slurry in fuel fired hydrolysis means.

7. The method of claim 6 including the step of operating said hydrolysis means at a temperature for raising the temperature of said slurry to about 300-400°

F. in about 2-5 minutes.

8. The method of claim 4 wherein said slurry is hydrolyzed at a pressure sufficient to suppress vaporization of said slurry.

9. The method of claim 8 wherein said pressure is about 67-415 psia.

10. The method of claim 4 wherein said step of further processing effluent from said step of hydrolyzing includes the steps of distilling effluent from said hydrolyzing step to form ethyl alcohol vapor, and feeding said vapor to packed vacuum distillation tower means for producing anhydrous ethyl alcohol.

11. The method of claim 4 wherein said biomass consists essentially of citrus peel.