AUSTRALIA Patents Act COMPLETE SPECIFICATION (ORIGINAL) Class Int. Class Application Number: Lodged: Complete Specification Lodged: Accepted: Published: Priority Related Art: Name of Applicant: Clear Water Technologies, Inc. Actual Inventor(s): Delman R. Hogen, Timothy France Address for Service and Correspondence: PHILLIPS ORMONDE & FITZPATRICK Patent and Trade Mark Attorneys 367 Collins Street Melbourne 3000 AUSTRALIA Invention Title: PROCESS FOR PRODUCING ETHYL ALCOHOL FROM CELLULOSIC MATERIALS Our Ref : 842445 POF Code: 193439/490141 The following statement is a full description of this invention, including the best method of performing it known to applicant(s): -1- PROCESS FOR PRODUCING ETHYL ALCOHOL FROM CELLULOSIC MATERIALS FIELD OF THE INVENTION 5 The present invention relates generally to the production of ethyl alcohol by yeast fermentation of fermentable sugars produced as a result of saccharifying cellulosic materials. BACKGROUND OF THE INVENTION 10 With the ever increasing world wide consumption of fossil fuels, there has been an ever increasing interest in alternative energy options. Considerable interest has now been focused on the use of ethanol. Ethanol has been found to have widespread application in beverages and food, as an industrial chemical, as a gasoline additive, and now, even more importantly, 15 as a fuel or gasoline replacement. Ethanol produces less toxic air emissions such as carbon monixide, CO, than the hydrocarbon fossil fuels currently used. Furthermore, ethanol has the advantage of being a renewable resource, as opposed to fossil fuel oil which is finite. Use of ethanol can also reduce the nation's dependence on these finite and largely foreign fossil fuel sources. However, efficiently producing ethanol in 20 sufficient quantities remains a concern. Various sources and methods of ethanol production have been attempted to date. There has been an increasing interest in the use of cellulose waste or by products as a source of ethanol production because these materials are often simply disposed of. Examples of such materials include the waste or by-products produced as a 25 result of harvesting agricultural crops such as the stalks, hulls or husks from legumes, or waste from cows or bovines. After harvesting, for example, the unwanted hulls and husks of legumes may be used as animal feed or field spread for easy disposal. Animal wastes may also be field spread for easy disposal. It has become desirable to employ such cellulose by product materials for conversion to ethanol, particularly in light of the 30 rising cost of fossil fuels. Cellulose is a polymer of D-glucose molecules linked together via p-1,4 linkages. Prior to fermentation, these polymers are cleaved or depolymerized to form simple sugars. This process is sometimes referred to in the art as saccharification. 2 Cellulose, however, is very resistant to cleavage. Thus, it can be challenging to accomplish the conversion in an efficient, economic manner so as to produce sufficient quantities of sugars which can then be fermented to ethanol. However, once cellulose is converted to fermentable sugars such as glucose, the 5 resulting sugar is easily fermented to ethanol using yeast. Thus, the difficult challenge of the process is to convert the cellulose to yeast fermentable sugars such as glucose. Commonly employed methods of saccharification include acidic and enzymatic hydrolysis, and mechanical degradation, the latter typically being employed in combination with one of the other methods. 10 Acid hydrolysis involves the use of either concentrated or diluted mineral acids. In concentrated form, the acids can produce high yields of fermentable sugars such as glucose, are expensive and cause difficulties for disposal of the waste acid material. To improve the overall yield of acid hydrolysis using diluted acids, pretreatment of the cellulose has been employed, and/or enzymatic hydrolysis. 15 Pretreatment involves mechanically and/or chemically treating the cellulose in order to break down the integrity of the fiber structure of the cellulose in order to make it more susceptible to attack by cellulose enzymes. Mechanical treatment may involve pressure, grinding, milling agitation, shredding, compression/expansion, etc. Sonification or ultrasound are commonly 20 employed in pretreatment of cellulose. Chemical methods involve the use of steam, acids or solvents. Many such pretreatment processes may leave a muddy pulp and undissolved solids. Adding enzymes, on the other hand, improves the efficiency of the process, but significantly increases the cost of production making it economically 25 inefficient for large scale production operations. A further complication is that yeast have a limited ability to ferment sugars other than glucose. Many methods of converting cellulose to glucose, such as acid hydrolysis, produce sugars, in addition to glucose, such as xylose in rather large quantities, which are not yeast fermentable which further decreases the efficiency of the 30 process. There is a continuing need for efficiently and economically converting cellulose to yeast fermentable sugars which can then be fermented to ethanol. The art referred to and/or described above is not intended to constitute an admission that any patent, publication or other information referred to herein is "prior 3 art" with respect to this invention. In addition, this section should not be construed to mean that a search has been made or that no other pertinent information as defined in 37 C.F.R. § 1.56(a) exists. All US patents and applications and all other published documents 5 mentioned anywhere in this application are incorporated herein by reference in their entirety. Without limiting the scope of the invention a brief summary of some of the claimed embodiments of the invention is set forth below. Additional details of the summarized embodiments of the invention and/or additional embodiments of the 10 invention may be found in the Detailed Description of the Invention below. A brief abstract of the technical disclosure in the specification is provided as well only for the purposes of complying with 37 C.F.R. 1.72. The abstract is not intended to be used for interpreting the scope of the claims. 15 SUMMARY OF THE INVENTION The present invention relates to an improved process for efficiently and economically producing ethanol and 2-propanol, and acetone from cellulose by fermentation of sugars produced as a result of saccharification of the cellulose without using acid hydrolysis, without using additional enzymes, and without mechanical or 20 other pretreatment. More particularly, the present invention relates to a process of converting cellulose to fermentable sugars using an inoculum of ethanologenic microorganisms, without additional enzymes, and then fermenting the fermentable sugars to ethanol using a yeast consortium which includes yeast, fungi or mixtures thereof. 25 According to the invention, cellulose is converted to fermentable sugars via enzymatic hydrolysis using enzymes which are produced by the ethanologenic microorganisms. The consortium of ethanologenic microorganisms may include bacteria, fungi or mixtures thereof. 30 Suitably the microorganisms are those that use a carbon source as an electron donor and Fe+ 3 as an electron acceptor. One source of iron which may be employed herein is magnetite. 4 Examples of suitable microorganisms include, but are not limited to, Enterobacter cloacae, Geobacter metalloreducens, Clostridium species, Pseudomonas species or mixtures thereof. In a preferred embodiment, at least Enterobacter cloacae is employed in 5 the consortium. The consortium of ethanologenic microorganisms are capable of converting cellulose to cellobiose, glucose, maltose or mixtures thereof. The resultant fermentable sugars can then be yeast fermented to ethanol using a consortium of yeast, fungi or mixtures thereof. 10 The invention is not limited by the yeast which may be employed herein and any suitable yeast finds utility herein. A small amount of oxygen may be added to the mix in order to discourage the growth of Methyl bacter which would produce methane under strictly anaerobic conditions. Alternatively, if the production of methane is desired, oxygen can 15 be excluded and the fermentable sugars can be anaerobically digested to produce methane. The exclusion of oxygen encourages the growth of Methyl bacter and can drive the pathway toward formation of methane. Methane can be employed for operation of any gas appliances that use natural gas, for instance, such as stoves, furnaces, and gas dryers. 20 The ethanologenic microorganisms for saccharification and the yeast consortium for fermentation may be added step-wise, or may be added to the cellulose simultaneously. Sources of cellulose include, but are not limited to, leafy plants, legumes, cane sugar, sugar beets, amylaceous grains and tubers such as corn, sorghum, wheat, 25 potatoes, rice, mylo, and the like. Cellulose by-products or waste material are particularly suitable for use herein such as those derived from agricultural harvesting or processing agricultural products such as hulls, husks, stalks, pulp, etc. as well as animal waste. The present invention has been found to greatly improve the yield of 30 ethanol which can be obtained from the fermentation of such products to ethanol or methane, for example. These and other aspects, embodiments and advantages of the present invention will become immediately apparent to those of ordinary skill in the art upon review of the Detailed Description and Claims to follow. 5 BRIEF DESCRIPTION OF THE DRAWINGS FIG. l is a block flow diagram illustrating the conversion of to ethanol in a specific embodiment which employs a bacterium to convert the cellulose to cellobiose, glucose and or maltose, and subsequent fermentation of these sugars with a yeast/fungal 5 consortium. FIG. 2 is a block flow diagram similar to FIG. I wherein the same process is shown to produce 2-propanol. FIG. 3 is a block flow diagram similar to FIGS. 1 and 2 wherein the same process is shown to produce methane. 10 FIG. 4 is a graph illustrating conversion of sugar beet pulp to maltose, subsequently to d-glucose and ultimate fermentation to ethanol. DETAILED DESCRIPTIONS OF THE PREFERRED EMBODIMENTS While this invention may be embodied in many different forms, there are 15 described in detail herein specific embodiments of the invention. This description is an exemplification of the principles of the invention and is not intended to limit the invention to the particular embodiments illustrated. All published documents, including all US patent documents, mentioned anywhere in this application are hereby expressly incorporated herein by reference in 20 their entirety. Any copending patent applications, mentioned anywhere in this application are also hereby expressly incorporated herein by reference in their entirety. This invention relates to the production of ethanol, particularly ethanol for use as a fuel, by saccharification of cellulose using ethanologenic microorganisms to produce fermentable sugars, followed by fermentation of the fermentable sugars to 25 produce ethanol and 2-propanol, and acetone. In a broad sense, the method according to the invention includes a saccharification step in which a consortium of ethanologenic microorganisms including at least one species of microorganism which uses carbon as an electron donor and Fe+ 3 as an electron receptor, expresses enzymes which hydrolyze the cellulose to fermentable 30 sugars. Fermentation can then be accomplished via a consortium of microorganisms including at least one species having the ability to ferment the fermentable sugars produced during the saccharification step, to ethanol. Alternatively, the process can be conducted anaerobically, and methane gas may be produced. 6 The term "consortium" as used herein, may refer to one or more species of microorganisms such as in a culture or inoculum. Any suitable source of cellulose may be employed herein. Sources of cellulose include, but are not limited to, grain, tubers, vegetative sources, fruit, leafy 5 plants, sugarcane and wood. More particularly, suitable sources include, but are not limited to, beets, corn, sorghum, wheat, potatoes, rice, mylo, and the like. Sources of cellulose for hydrolysis to fermentable sugars are discussed in U.S. Patent Nos. 6,660,506 and 6,423,145, each of which is incorporated by reference herein in its entirety. 10 The present invention finds particular utility in converting cellulose by product material or cellulose waste to ethanol via enzymatic hydrolysis followed by yeast fermentation. The enzymes are produced by the ethanologenic microorganisms. The cellulose is saccharified to the fermentable sugars, cellobiose, glucose, maltose or mixtures thereof. 15 By-products or waste from harvesting and processing of field crops are particularly advantageous for use in the process disclosed herein because such by products or waste are typically disposed of. For example, hulls, husks, stalks, pulp from such products may be spread on a field for disposal or used as animal food usually low nutrition and cost. Cow and bovine manure are also commonly disposed of by spreading 20 onto a field. As used herein, the term "by product" shall refer to a variety of sources of cellulose including, but not limited to, hulls or husks from a variety of agricultural products such as legumes, stalks, leaves, animal waste, etc., which are often discarded and as such, find particular utility in the processes described herein. For example, 25 suitable by product sources include, but are not limited to, sugar beet hulls and soy bean hulls, by product sugar beet pulp, spent corn mash, corn husks and corn stalks, etc. Examples of animal waste which can be employed herein include the waste from cows or bovines. Cow manure has a cellulose content between about 50 wt % to about 75 wt-%, more typically, cow manure is roughly 2/3 cellulose based on its 30 total weight. Turning now to the figures, FIGS. 1-2 are block flow diagrams illustrating the process of converting cellulose derived from sugar beet pulp, a by product obtained as a result of processing of sugar beets, to ethanol, 2-propanol or methane, according to the invention. Using sugar beet pulp is advantageous for ethanol 7 production due to the enormous quantity of this pulp produced as a by-product of the sugar beet processing industry. Referring to FIG. 1, in a first step, cellulose, derived from sugar beet pulp produced as a by-product of sugar beet harvesting and processing, is added to water in 5 amounts between about 5% and 25% cellulose with the remainder being water. In this embodiment, a consortium of microorganism including Enterobacter cloacae, along with a source of Fe' , was added to the cellulose/water mixture. Enterobacter cloacae can be added in amounts of about 0.05% to about 1%, more typically about 0.1% to about 0.5% by volume. For example, 1000 ml of cellulose/water mixture can be inoculated with I 10 ml of microbial consortium. These ranges are intended for illustrative purposes only, and not as a limitation on the scope of the present invention. While the embodiment shown in FIGS. 1-2 employs a consortium including the species Enterobacter cloacae, other suitable microorganisms may also be employed and include, but are not limited to, members of the genus clostridium, 15 members of the genus Pseudomonas, the species Geobacter metalloreducens, and the species Shewanella putrefaciens, for example, as well as mixtures thereof. Suitably, the bacteria are mesophilic, thriving in mid-range temperatures of about 250 C to about 35 *C. A source of iron may be added in amounts of about 0.05% to about 1%, 20 and more typically about 0.1% to about 0.5% by weight to act as an electron acceptor for the Enterobacter cloacae. Enterobacter cloacae is an oxidative organism that operates well under anaerobic conditions, i.e. typically 85% to 95% substrate reduction is achieved only a small amount of oxygen may be added to shut down the Methyl bacter. Other suitable electron acceptors may also be employed and include, but are not limited 25 to, nitrate (NO 3 ) and oxygen (02), as well as combinations of any suitable electron acceptors as well. The ranges are intended for illustrative purposes only, and not as a limitation on the scope of the present invention. The electron donor is the beet pulp cellulose. The electron acceptor along with a micro-oxidative environment, encourage the p-1,4 linkages of the D-glucose units 30 to break, i.e. via enzymatic hydrolysis, thereby producing cellobiose. The enzymes are produced by the ethanologenic microorganisms. No commercial enzymes are added. The oxidation reduction potential of the reaction may range from about 65 millivolts to about -110 millivolts. 8 It is surmised that the cellobiose is further hydrolyzed to glucose and/or maltose. It is believed that the maltose is produced by partial hydrolysis of cellulose, or from the partial hydrolysis of pectin. Glucose is then fermented to ethanol while maltose is fermented to 2-propanol. Small amounts of acetone are also provided in the 5 reange of about .0% to .3% Consumable agricultural, i.e. plant, materials, may be composed of cellulose (a p-1,4-linked glucose polymer), hemicellulose (made up of polymers containing -1,4-linked galactose and mannose), pectin (an a-1,4-linked polygalacturonic acid) and lignin (a polysaccharide phenolic polymer made up of a variety of phenylpropanes and guaiacyl, syringyl, p-hydroxyphenyl, and biphenyl 10 nuclei.). One suitable source of iron is magnetite (iron oxide, Fe304). The microorganisms can be cultured using any suitable culturing medium as is known in the art. Brewer's thioglycollate medium is one example of a suitable culturing medium. 15 The contents are suitably mixed for 24 hours or as required. The pH is suitably between about 5 and 7 and more suitably between 5.5 and 6.5. In the embodiment illustrated by FIG. 1, Enterobacter cloacae functions to produce enzymes for enzymatic hydrolysis of cellulose to cellobiose, a disaccharide (i.e. two glucose moieties in B-(1,4-linkage) which forms the basic repeating unit of 20 cellulose and obtained by partial hydrolysis of the polysaccharide. Enterobacter cloacae has been found by the present inventors to very effectively and efficiently cleave cellulose bonds to produce cellobiose. The cellobiose is further hydrolyzed to glucose and/or maltose, maltose also a disaccharide, which can then be fermented using a yeast and/or fungal consortium to produce ethanol and 2-propanol. While glucose is primarily 25 fermented to ethanol and a small amount of acetone, it is believed that maltose is primarily fermented to 2-propanol (FIG. 2). Any yeast and/or fungi suitable for fermentation of these simple sugars can be employed herein, and certain species of bacteria have also been found to be suitable for fermentation of the simple sugars. Examples of suitable yeast include, but 30 are not limited to, species from the genus Saccharomyces such as Saccharomyces cerevisiae and Saccharomyces pombe, Zymomonas mobilis, and species from the genus Brettanomyces such as Brettanomyces custersii and Brettanomyces bruxellensis, etc. Examples of suitable yeast and/or fungi can be found in U.S. Patent Nos. 4321328 (Sacchromyces Cerevisiae), 5100791 (Brettanomyces custersii), 6569653, each of which 9 is incorporated by reference herein in its entirety. These are intended for illustrative purposes only, and not as a limitation on the scope of the present invention. The invention is not limited by the type of yeast which may be employed providing the yeast can ferment cellobiose, glucose, maltose, or mixtures thereof. 5 Some bacteria can also ferment simple sugars. See, for example, U.S. Patent Nos. 4647534, 4731329, 4830964, each of which is incorporated by reference herein in its entirety. Preferable for use herein are those yeasts capable of fermenting glucose and/or maltose, or cellobiose if any is left, to ethanol. However, it would appear that the 10 cellobiose is hydrolyzed to glucose and/or maltose during the saccharification step. In the embodiment shown in FIGS. 1-2, a consortium including Saccharomyces cerevisiae has been found to be preferable for use in fermentation of the simple sugars produced as a result of saccharification of the cellulose beet pulp. Fermentation may be suitably allowed to proceed for about 48 hours or as 15 needed to either complete the fermentation process or to reach the desirable levels of ethanol production. FIG. I illustrates a pathway for which ethanol is produced via saccharification of cellulose to cellobiose and glucose, and subsequent fermentation of glucose to ethanol. However, it has been found that 2-propanol and acetone may also be 20 produced. With the addition of oxygen in amounts sufficient to discourage the growth of bacteria which produce methane, such as Methyl bacter, it has been found that ethanol is produced in amounts of about 10% to about 20%, 2-propanol in amounts of about 1% to about 10%, and acetone in amounts of about 0.1 % to about 1%. Carbon dioxide is given off as a by-product. Oxygen may be added in small amounts of a few parts per 25 billion to a few parts per trillion. The process embodied in FIG. I has been found to produce 12.5% by weight ethanol (FIG. 1), 5% by weight of 2-propanol (FIG. 2), and 0.3% by weight of acetone with a I liter sample. This is a substantially high yield of ethanol based on the initial amount of 30 cellulose employed. Alternatively, oxygen may be excluded from the process. In the event that oxygen is excluded, the growth of Methyl bacter may not be hindered, and methane may be produced. This process is shown as a blow flow diagram in FIG. 3. The process illustrated in FIG. 3 has been found to produce yields of methane as high as 80% by 10 weight and 20% carbon dioxide. The range may be anywhere from about 40% to about 80% by weight methane yield. In FIGS. 1-3, the cellulose source is sugar beet pulp. Some sources of cellulose, such as sugar beet pulp, appear to be more readily hydrolyzed by these 5 enzymes than other sources. For cellulose from sources which are more difficult to hydrolyze, a solvent may first be employed to begin cleavage of the cellulose. Suitable solvents include, for example, a-hydroxy acids or salts thereof, transition metal halides or oxides, and mixtures thereof. For example, in one embodiment, a mixture of citric acid or sodium salt 10 thereof, and ferric chloride (FeCIA), is employed to begin hydrolysis of the cellulose. After addition of the solvent, the mixture may be heated to further induce hydrolysis of the cellulose. The present invention can be adapted to either batch processing, or to continuous processing, such as by a zone mixed, plugged flow digester. 15 After processing, centrifugation can be employed to separate the liquid from any remaining solids, followed by distillation to obtain ethanol. In one embodiment, double distillation, followed by treatment with a molecular sieve to take off any remaining water, was employed to obtain a pure ethanol product. 2-propanol and some acetone may also be obtained with this procedure. 20 Molecular sieves can be advantageously regenerated and recycled using alternating tanks. The present invention offers several advantages over currently employed methods of producing ethanol. One advantage is that the process does not require acid hydrolysis. Therefore, there is no problem with disposal of waste acid. 25 Further, the process according to the invention does not require the addition of any commercially generated enzymes. The enzymes employed are produced by the ethanologenic microorganisms. As commercially generated enzymes are expensive, the process according to the invention is more economical than those methods which do require additional commercial enzymes. 30 Yet another advantage in employing the method according to the invention is that saccharification and fermentation can be conducted in a single fermentation reactor if so desired. In a typical process, cellulose is treated with commercially extracted enzymes wherein optimum reactivity for saccharafication is conducted under conditions of pH, oxidation potential and/or temperature, which is not 11 conducive to yeast propagation. Therefore, the fermentation is typically conducted in another reactor. A further advantage is the ability to be able to switch between producing ethanol or methane by the simple process of adding a small amount of oxygen for 5 ethanol production and by excluding oxygen for methane production. The process according to the invention also advantageously employs by products from harvesting agricultural products which are very abundant. The current invention is further illustrated by the following non-limiting examples. 10 Example I Example I illustrates a process whereby a microbial and fungal consortium was employed to produce high grade ethanol and 2-propanol from by product sugar beet pulp. 15 The microbial inoculum was first prepared by adding approximately I ml of a stock solution including Enterobacter cloacae to 25 g of Brewer's thioglycollate medium and autoclaving at 1200 C for about 45 minutes. The medium is then cooled to about 30* C. Mass doubling time for the bacteria is approximately 15-20 minutes. After 24 hours, the bacterial population in the culture is approximately I x 108 to about I x 20 10 9 . Sugar beet pulp was mixed with water at a ratio of 25% sugar beet pulp to 75% water to produce an aqueous sugar beet pulp mixture. Sucrose and other constituents were harvested from the aqueous sugar beet pulp mixture leaving cellulose, hemi cellulose, and pectin. 25 A 1 liter sample was spiked at initiation with 0.2 to 0.3 milliliters of molasses per liter and glucose in an amount of 0.8 gram per liter of the aqueous sugar beet pulp mixture. From this point on, the ethanol generation process ran by itself without glucose supplement. Molasses was added only at startup. The sugar beet pulp falls apart at the end of the hydrolysis. 30 As determined by High Performance Liquid Chromatography (HPLC), ethanol was obtained in an amount of about 3 grams of ethanol per liter of the aqueous sugar beet pulp mixture, or about 12.5% based on the total weight of ingredients put into the system. 12 A small amount of oxygen, from parts per billion to parts per trillion, was added to the process to inhibit the growth of methanogens such as Methyl bacter. Methanogens produce methane gas at the expense of ethanol production. Thus, exclusion of all oxygen can drive the system to methane gas production. 5 If so desired, methane gas can be generated by preventing oxygen inclusion in the reactor. Table I illustrates the various components produced and the amount of each one produced over a 10 day period. 10 TABLE 1 PERCENT BY WEIGHT Day dp3 MALTOSE d-GLUCOSE GYCEROL ETHANOL 2-PROPANOL 1 0.02 0.01 0.00 0.00 0.00 0.00 2 0.64 0.01 0.02 0.00 0.33 0.00 3 0.08 0.00 0.00 0.08 0.38 0.01 4 0.00 1.02 0.00 0.00 0.32 0.19 5 0.91 0.00 0.00 0.02 1.10 0.01 6 0.00 1.27 0.00 0.00 0.99 0.21 7 0.00 1.45 0.00 0.00 0.75 0.26 8 0.00 1.55 0.00 0.00 1.29 0.37 9 0.00 1.35 0.00 0.00 2.09 0.48 10 0.00 1.38 0.00 0.00 2.10 0.47 FIG. 4 is a graph showing the results of Example 1. The process exhibited about 85 % efficiency providing an ethanol yield of 43 %, and a 2-propanol 15 yield of 9.6 % by weight based on the total ingredient yield. The combined yield of alcohol is 52.4 % by weight, or 67 % by volume. The graph illustrates a 10 day run of ethanol production. HPLC was performed on the reaction mixture each day. The first cycle of the DP3 peak (3 carbon sugars) presented after 2 days. 20 It is from this source that ethanol was generated. Substantially all of the 3 carbon sugars were consumed as carbon source. The first cycle of maltose production appeared on day 4. The further hydrolysis of maltose generates two glucose molecules. The glucose was consumed so fast that it was not detectable after day 2. 13 The first ethanol peak appeared on day 2 and the first 2-propanol peak appeared on day 3. A second peak representing the 3-carbon sugars appeared on the fifth day. A sharp increase in ethanol production accompanied the production of 3-carbon 5 sugars. From the sixth day on, the ethanol generated relied on the elevated hydrolysis of maltose. Example 2 10 It has been found that the maximum amount of ethanol which can be produced is limited by the yeast fermentation. Above about 12.5% ethanol, by weight of the total reactor ingredients, the yeast is poisoned by its own ethanol discharge and 2 propanol production begins. Therefore, the amount of cellulose placed into the system was decreased 15 for example 2. The bacteria were cultured as described for Example 1, above. The following ingredients were employed: 20 900 g distilled water 100 g cellulose (sugar beet pulp) Phosphorous and nitrogen were added 20 g yeast extract 1 g magnetite 25 10 g molasses 8 g dextrose 25 g Brewer's thioglycollate medium with bacteria 10 g Bacto-peptone protein source 30 The following steps were followed: 1. The Brewer's thioglycollate medium was autoclaved at 1200 C for 45 minutes. 2. The medium was allowed to cool to 30* C. 3. The reactor, having the remaining ingredients, was inoculated with the medium 35 having the bacteriological consortium at a pH between about 5.5 and 6.5 4. The total mixture was incubated at 300 C in a shaker bath with a cap held loosely on the vessel for 3 days. 5. For ethanol, 2-propanol and acetone production incubation was continued for another week. 40 14 If methane production is desired, a gas-lock can be added to the reaction vessel after step 4 to exclude oxygen, and the reaction allowed to proceed anaerobically. HPLC was employed to analyze the product. The resultant product had 12.5% ethanol, 5% propanol and 0.3% acetone. 5 The above disclosure is intended to be illustrative and not exhaustive. This description will suggest many variations and alternatives to one of ordinary skill in this art. All these alternatives and variations are intended to be included within the scope of the claims where the term "comprising" means "including, but not limited to". Those familiar with the art may recognize other equivalents to the specific embodiments 10 described herein which equivalents are also intended to be encompassed by the claims. 15