Method for pretreatment of cellulosic and lignocellulosic materials for conversion into bioenergy

• US 8,449,773 B2
• Filed: 07/06/2010
• Issued: 05/28/2013
• Est. Priority Date: 07/06/2009
• Status: Expired due to Fees

• Current Assignee: Brigham Young University (The Church of Jesus Christ of Latter-Day Saints)
• Original Assignee: Brigham Young University (The Church of Jesus Christ of Latter-Day Saints)
• Inventors: Hansen, Jaron C., Hansen, Lee D.
• Primary Examiner(s): Desai, Anand
• Assistant Examiner(s): LIU, SAMUEL W
• Application Number:
  US12/863,439
• Publication Number:
  US 20110117619A1
• Time in Patent Office: 1,057 Days
• Field of Search: None
• US Class Current: 210/627
• CPC Class Codes: C10G 1/00 Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal mechanical winning of oil from oil-shales, oil-sand, or the like B03B
• CPC Class Codes: C10G 1/047 Hot water or cold water extraction processes
• CPC Class Codes: C12P 2201/00 Pretreatment of cellulosic or lignocellulosic material for subsequent enzymatic treatment or hydrolysis
• CPC Class Codes: C12P 3/00 Preparation of elements or inorganic compounds except carbon dioxide recovery of carbon dioxides as by-products C12F3/02
• CPC Class Codes: C12P 5/023 Methane
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel
• CPC Class Codes: Y02W 10/37 using solar energy

Abstract

A process for converting organic waste materials into usable products and products thereof is disclosed. According to the process, organic waste materials are contacted with an oxidant to form a product and then an amount of the oxidant is removed from the product to form a reactor-ready feedstock. The oxidant is removed by various means, including washing, photolysis, catalytic means, oxidation of the oxidant, reduction of the oxidant, and heat. The reactor-ready feedstock may then be introduced into a reactor, such as a digester or incubator, and the reactor-ready feedstock is converted by microorganisms into biofuel or other products.

Claims

1. A process for treating organic materials in order to minimize the cost-benefit ratio of converting the organic material to biofuel;

the process comprises the steps of

a. providing an aqueous slurry comprising organic materials;

b. contacting said aqueous slurry with a solution comprising an amount of peroxide;

c. forming a mixture comprising said aqueous slurry and said solution, wherein the concentration of peroxide in said mixture is at least 1 ppm, said amount of peroxide being sufficient to oxidize at least a portion of said organic materials into an oxidized product and wherein said oxidized product comprises an amount of organic peroxide;

d. photolyzing at least a portion of said amount of said organic peroxide, thereby deactivating at least 5% of said amount of said organic peroxide wherein said photolyzing is accomplished by exposing said organic peroxide to wavelengths of an electromagnetic light in the range between 189 nm to 350 nm inclusive; and

wherein said oxidized product produces at least 50% less foam than said oxidized product would have without photolyzing said at least a portion of said amount of said organic peroxide; and

e. adding bacteria to said oxidized product.

2. The process of claim 1, further comprising the steps of

a. contacting said oxidized product with at least one microorganism in a reactor;

b. converting said oxidized product into a metabolic product, said metabolic product comprising a hydrocarbon gas; and

c. collecting said metabolic product.

3. The process of claim 1, further comprising the steps of

a. contacting said oxidized product with at least one microorganism;

b. converting said oxidized product into a metabolic product, said metabolic product comprising hydrogen gas; and

c. collecting said metabolic product.

4. The process of claim 2, wherein said hydrocarbon gas is at least one of the following selected from the group consisting of methane and hydrogen.

5. The process of claim 2, wherein said at least one microorganism comprises a methanogenic bacteria and wherein said hydrocarbon gas comprises methane.

6. The process of claim 1, further comprising the steps of

a. photolyzing at least a portion of said amount of peroxide for a first period of time;

b. photolyzing said organic materials for said first period of time, wherein the steps of photolyzing said at least a portion of said amount of peroxide and photolyzing said organic materials accelerates the rate at which said organic material is converted into oxidized product;

c. photolyzing at least a portion of said amount of peroxide for a second period of time; and

d. photolyzing at least a portion of said organic materials, wherein the steps of

     1) photolyzing said at least a portion of said amount of peroxide and

     2) photolyzing at least a portion of said organic materials decelerates the rate at which organic material is converted into oxidized product.

7. The process of claim 1, wherein said oxidized product is washed with at least one washing agent, wherein said at least one washing agent is selected from the group consisting of water, distilled water, deionized-distilled water, polar substances, catalysts, oxidizing agents, reducing agents, and combinations thereof.

8. The process of claim 1, wherein a ratio of moles of said peroxide to moles of said organic materials is at least greater than 1 mole of peroxide to 100 moles of organic material.

9. The process of claim 1, wherein said organic material comprises lignocellulosic material and the ratio of moles of peroxide to moles of lignocellulosic material in said organic material is greater than 1 mole of peroxide to 100 moles of lignocellulosic material.

10. The process of claim 9, wherein the step of photolyzing at least a portion of said amount of organic peroxide is accomplished by exposing said organic peroxide to wavelengths of electromagnetic light, wherein said wavelengths are greater than 189 nm and less than 401 nm.

11. The process of claim 9, wherein said organic materials comprises at least one of the following:

materials selected from the group consisting of food industry waste, animal waste, paper industry waste, municipal solid waste, tire waste, petroleum refining waste, and biomass.

12. The process of claim 1, wherein said peroxide is selected from the group consisting of hydrogen peroxide, peroxide, sodium percarbonate, sodium peroxycarbonate, sodium peroxide, calcium peroxide, organic peroxides, barium peroxide, superoxides, and any compound capable of producing a peroxide in water.

13. A method of producing methane from organic materials comprising the steps of:

a. providing an amount of organic material;

b. forming a slurry from the amount of organic material;

c. mixing the amount of the organic material with an amount of peroxide solution;

wherein said mixing generates a product which comprises an amount of organic peroxide;

d. combining the product with a chemical solution, wherein said combining produces a pretreated substance;

e. photolyzing at least a portion of said amount of organic peroxide, thereby deactivating at least 5% of said amount of organic peroxide, wherein said product produces at least 50% less foam than said product would have without photolyzing said at least a portion of said amount of said organic peroxide; and

f. incubating the pretreated substance in a reactor for a period of time sufficient to convert a portion of the product into an amount of methane.

14. The method of claim 13, wherein the product that has been substantially freed from organic peroxide contains a sufficiently low concentration of said organic peroxide, wherein said product is substantially free from foam when introduced into the reactor, wherein said reactor is selected from the group consisting of anaerobic reactors and partially-anaerobic reactors.