Method and system for processing a biomass for producing biofuels and other products

a biomass and biofuel technology, applied in the field of biomass processing, can solve the problems of not being a finite fuel source, reducing the greenhouse effect, and continuing the global energy crisis, and achieve the effects of high production costs, efficient and cost-effectively, efficient and cost-effectiv

Inactive Publication Date: 2012-05-17
EL SHAFIE MOUSTAFA AHMED
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  • Summary
  • Abstract
  • Description
  • Claims
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AI Technical Summary

Benefits of technology

[0012]In view of the limitations associated with the production of first and second generation biofuels, including the food vs. fuel conflict of first generation biofuels, and the high production costs associated with second generation biofuels, there is clearly a need in the art for new methods of efficiently and cost-effectively producing alternative fuels without taxing the environment or competing with food production. The present invention solves this problem by providing an efficient and cost-effective method to produce products useful in biofuels and other products.

Problems solved by technology

The global energy crisis is continuing to grow as fossil fuels are facing their inevitable depletion.
Substituting biofuels for fossil fuels will decrease the greenhouse effect, and with a steady, sustainable, and uninterrupted supply, biofuels will not be a finite fuel source.
However, liquid biofuels generated thus far have their own difficulties and concerns that need to be addressed and overcome.
Therefore, first generation biofuels compete with human and animal nutrition for agricultural crops, because these crops are produced on a limited amount of land.
This limited amount of farm land cannot satisfy both global food and fuel needs, thereby generating the food vs. fuel conflict.
Accordingly, first generation biofuels are limited by competition with food crops for land and cannot be abundant enough to become widely available, thus preventing the adoption of alternative fuels.
In addition, algae consume the greenhouse gas carbon dioxide and produce the globally needed oxygen as a metabolic waste product.
However, the selection of lignocellulose and algae as starting materials introduced a new set of problems.
In particular, generating ethanol from lignocellulose has a number of technical problems.
Delignification of lignocellulose to liberate cellulose and hemicellulose from their complex with lignin is the rate-limiting and most challenging step in the production of ethanol from lignocellulose (Lin and Tanaka.
In addition, depolymerization of the carbohydrate polymers (e.g., acid hydrolysis of the cellulose from wood) destroys most of the desired materials, simple fermentable sugars, in the process.
Also, the fermentation of hexose and pentose sugars together generates a low ethanol yield.
Hydrolysis of lignocellulose feedstock via high temperatures, acid treatment, and / or high pressure is also a complex energy consuming process.
In addition to, and due in part to, the technical problems of generating lignocellulosic ethanol, its production cost is high despite the fact that lignocellulose is an inexpensive agricultural residue when compared to the starch-based agricultural products used in the production of first generation biofuels.
Also, the costly initial investment to convert or build a lignocellulose refinery would result in a small number of lignocellulose refineries, high freight costs for delivering bulky cellulose long distances to the limited number of refineries, very large and costly storage areas to contain the biomass, and a large output of residual waste.
The high cost of lignocellulosic ethanol, the drastic drop in oil prices at the end of 2008, and the global economic crisis contributed in putting many lignocellulosic ethanol projects on hold and leading to a reluctance to invest in ethanol projects.
Additionally, since the mid-1970s, extensive research has been carried out in the field of lignocellulosic ethanol production; however, the first lignocellulosic ethanol fuel plant was not operational until 2004 in Canada.
Although the lipids derived from algae are readily converted to biodiesel by known methods, and lipid extraction via oilseed extraction is available (see, e.g., U.S. Pat. No. 4,456,556), the cultivation of algae is challenging.
For example, growing algae in an open-pond system is much less expensive than growing algae in a closed photobioreactor system; however, the open-pond system is open to contaminants, and it is more difficult to provide optimal amounts of carbon dioxide and light while maintaining the temperature and pH to achieve maximum growth of the algae in an open-pond.
Thus, stimulating exponential growth of algae in a closed or open system is costly, and cultivating algae on a commercial scale is exceedingly difficult.
Bioreactors have proven to be most effective in producing high quality algae at the greatest rate, but they are expensive, and it has yet to be shown that algae are economically feasible for commercial scale production (see, e.g., Benemann, Opportunities and Challenges in Algae Biofuels Production [online], [Retrieved on Jun. 22, 2009].

Method used

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  • Method and system for processing a biomass for producing biofuels and other products
  • Method and system for processing a biomass for producing biofuels and other products
  • Method and system for processing a biomass for producing biofuels and other products

Examples

Experimental program
Comparison scheme
Effect test

example 1

Generation of a Biomass

[0211]This example describes one exemplary method of generating a biomass.

[0212]In order to generate a biomass, the fungus Aspergillus fumigatus was utilized as the microorganism, and well-chopped rice straw, a lignocellulosic material, was provided as the biodegradable substrate. 10 g of rice straw was placed in each of 10 flasks. The rice straw was washed and dried in the flask, and the weight of the clean, dry straw was recorded (see Table 1). The percentage of weight lost by the rice straw due to washing and drying was calculated. Once the dry weight of the clean straw was recorded, 200 ml of water was added to each flask.

[0213]Glycerol (0.1 ml / flask) and urea (0.01 g / flask) were added to the rice straw as nutritional supplements. Glycerol was chosen as a supplement, because it is a byproduct of biodiesel production, and using glycerol as a supplement is one way to recycle this abundant, inexpensive, and readily available byproduct. Urea, a common componen...

example 2

Autolysis Induction

[0217]This example describes one exemplary method of inducing autolysis of a biomass.

[0218]In order to induce autolysis of the A. fumigatus biomass, the mycelia biomass generated in Example 1 were first collected for chopping and grinding to increase the exposed surface area. After being chopped, the biomass was returned to the liquid media, and 0.2 to 0.4 g of a chlorine dioxide tablet was dissolved in the media. The biomass was exposed to the chlorine dioxide for 5 to 15 minutes to induce autolysis. Following the exposure time, the flask was agitated for about 5 to 10 minutes to let the air penetrate into the solution and decompose the chlorine dioxide. Next, the flask was incubated in UV light for about 5 minutes to decompose any remaining chlorine dioxide and sterilize the flask. Hydrogen peroxide (1.5 ml of 30% H2O2 / liter of media) was then added to inhibit glucose oxidase, bleach any dyes in the biomass, and kill any surviving microorganisms. After a 1 hour ...

example 3

Characterization of Fatty Acids and Other Products in Autolysate

[0219]This example demonstrates the production of fatty acids and other useful products using two different fungal strains according to methods of the present invention.

[0220]Briefly, 30 flasks were washed and sterilized. Culture media was prepared containing 0.5 ml of glycerol, 0.05 grams of urea, and 0.1 grams of chlorine dioxide dissolved in 1000 ml of water. 200 ml of culture media was distributed to each flask. 5 grams of well-chopped rice straw was added to each flask, where it soaked in the culture media for 10 minutes. The flasks were then agitated for 5 minutes, following which the flasks were placed under UV lamps for 10 minutes. The flasks were then inoculated with spores; 15 flasks were inoculated with Aspergillus fumigatus spores, and 15 flasks were inoculated with Trichoderma viride spores. All flasks were incubated for 6 days at 29±1° C.

[0221]Following incubation, fresh mycelia were collected and weighed....

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Abstract

The present invention provides methods of processing a biomass, e.g., for producing lipid and non-lipid materials, by inducing autolysis of a biomass. The biomass may be generated using any species of microorganism and any available biodegradable substrate, including waste materials. The lipid and non-lipid materials are present in two separate layers of the autolysate, and they can be used to generate valuable products such as biofuels and nutritional supplements. The present invention further provides a processing apparatus useful for practicing the methods of the present invention.

Description

CROSS-REFERENCE TO RELATED APPLICATION[0001]This application claims the benefit under 35 U.S.C. §119(e) of U.S. Provisional Patent Application No. 61 / 223,995 filed Jul. 8, 2009, where this provisional application is incorporated herein by reference in its entirety.BACKGROUND OF THE INVENTION[0002]1. Field of the Invention[0003]The present invention relates generally to methods of processing a biomass to obtain useful lipid and non-lipid materials, including intermediates for producing biodiesel and ethanol. In particular embodiments, a microorganism is grown on a biodegradable substrate and the resulting biomass is induced to undergo autolysis, thus releasing the lipid and non-lipid materials from the biomass. The present invention is also directed to a processing system useful for practicing the methods of the present invention.[0004]2. Description of the Related Art[0005]The global energy crisis is continuing to grow as fossil fuels are facing their inevitable depletion. At the sa...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C12P7/64C12P7/02C12S3/00C02F3/00C11B3/02C01B31/20C01B3/22F01N3/20C12M1/36C01B32/50
CPCA23K1/007C12P2201/00C02F2303/06C02F2305/14C11B1/025C11B1/10C12M47/06C12N1/06C12P7/6409C12P7/6463C12P7/649Y02E50/13C02F3/00C12F3/02C12P3/00C12P7/64C02F3/34A23K10/12Y02E50/10Y02P20/145
Inventor EL-SHAFIE, MOUSTAFA AHMED
Owner EL SHAFIE MOUSTAFA AHMED
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