WO1996028400A1 - Biomass reduction and bioremediation processes and products - Google Patents
Biomass reduction and bioremediation processes and products Download PDFInfo
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- WO1996028400A1 WO1996028400A1 PCT/US1996/003775 US9603775W WO9628400A1 WO 1996028400 A1 WO1996028400 A1 WO 1996028400A1 US 9603775 W US9603775 W US 9603775W WO 9628400 A1 WO9628400 A1 WO 9628400A1
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- bioremediation
- pile
- situ
- water
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09C—RECLAMATION OF CONTAMINATED SOIL
- B09C1/00—Reclamation of contaminated soil
- B09C1/10—Reclamation of contaminated soil microbiologically, biologically or by using enzymes
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
- C05F17/10—Addition or removal of substances other than water or air to or from the material during the treatment
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
- C05F17/50—Treatments combining two or more different biological or biochemical treatments, e.g. anaerobic and aerobic treatment or vermicomposting and aerobic treatment
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F9/00—Fertilisers from household or town refuse
- C05F9/04—Biological compost
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09C—RECLAMATION OF CONTAMINATED SOIL
- B09C2101/00—In situ
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/145—Feedstock the feedstock being materials of biological origin
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Definitions
- This invention relates to the field of biomass remediation or composting processes for the production of a useful microbial product for either subsequent bioremediation processing of various substrates or direct application to soil as an agricultural fertilizer.
- the process involves a thermophilic alkalinophilic reaction, involving predominantly aerobic microbes, which stresses the microbial population in the presence of high moisture and high pH conditions during an initial reaction step and wherein subsequent reaction at high moisture, lower pH and added nutrients enables the surviving microbial population to perform a composting operation in a novel operation wherein the aerobes break down or digest the waste substrate materials without conventional stirring, turning or agitation of the compost pile to aerate it and without the need for otherwise directly introducing air or oxygen by conventional mechanical devices such as pumps or blowers.
- This invention also relates to the field of bioremediation of contaminated soils or other industrial wastes and the production of valuable fatty acids and amino acids.
- Such contamination by seepage is not at all limited to municipal waste disposal, and often occurs due to undesirable release or escape of hazardous materials from refineries, chemical manufacturing plants, manufacturing plants using, or having as waste by-products, various chemicals and paints, and is often due to spills occurring during transportation of hazardous materials.
- the present invention uses indigenous organisms, but the inventive processing steps achieve an enzymatically catalyzed reaction, which not only reduces the amount of turning to aerate the compost piles, or the expensive process of pumping air or oxygen into the pile, but also provides a very fast reaction process where the composting operation can be essentially completed in little more than a month which is typically unheard of in popular composting processes.
- the present invention both from a processing standpoint as well as in the use of derivatives from the basic composting operation is useful in solving many of the problems identified in the above articles, including but not limited to the breakdown and disposal of municipal solid waste, bioremediation of hazardous materials, safe breakdown and disposal of waste products at manufacturing sites, in situ bioremediation or surface contaminated soil, in situ bioremediation of subsurface soils and liquid bodies, breakdown of long chain carbon compounds into shorter carbon chain compounds, the derivation of useful amino and fatty acids at low cost as bioremediation byproducts and the generation of a pathogen free fertilizer as a composting byproduct with an improved plant nutrient retention time accompanied by improved water retention when applied to soil for agricultural purposes.
- FIGS. 1-4 are charts showing test results of the action of bacterial strains of the present invention on trichlorothylene (TCE);
- FIG. 5 illustrates two electrically interconnected subterranean wells connected to a DC power source and to a bacterial and nutrient supply tank;
- FIG. 6 is an expanded vertical section of the negatively charged well of FIG. 5;
- FIG. 7a is a plan diagram of multiple locations for electrically interconnected subterranean wells as in FIG. 5, arranged at the center of and in a circle for subsurface bioremediation;
- FIG. 7b is a plan diagram similar to FIG. 7a with the well locations at opposite sides of a rectangle;
- FIG. 8 is a vertical section through a tank used for bioremediating the hazardous waste toxaphene
- FIG. 9 is a diagrammatic section of a pit containing hydrocarbon contaminated soil and with a central tube for extracting bioremediation products
- FIG. 10 is a diagrammatic section of a bioreactor for disposing of manufacturing wastes or for manufacturing useful products by bioconversion. Description of Preferred Embodiments While not being bound by theory set forth herein as to why the processes and products detailed herein perform in unexpected ways and achieve unexpected results, it is believed that the initial step of stressing the bacteria population at high temperature and at high pH in the presence of high moisture in a compost pile results in, at the end of approximately two days, a substantially pathogenic-free population of bacteria having the capability of continuing to repopulate the pile and break down the waste products therein during a one to two month period after the initial stressing step.
- Water is also regenerated in the pile by the breakdown of organic compounds from which carbon combines with oxygen to form carbon dioxide and hydrogen combines with oxygen to form water.
- a deleterious hydrocarbon may be broken down as part of a composting operation using the present process or as a substrate specific material being acted upon by a similar process using bacteria derived from the composting process.
- the use of composting derived bacteria is preferable to provide a high degree of metabolic activity supported by the enzymatically catalyzed generation of oxygen to accelerate any bioremediation action.
- the process for producing these composting-derived bacteria can be repeated at will using readily available waste, sewer sludge, horse manure, water and indigenous bacteria combined as set forth elsewhere in this specification.
- the genus bacillus is one of the most studied microorganism genera, this invention has demonstrated the unique ability of strains of this genus of bacteria, found as end products of this invention, to not only be extremely prolific and rapidly populate (see FIG. 8), but also to have properties of their enzymes for catalyzing a reaction involving water, nutrients and contaminated substrates to provide biomass degradation and bioremediation that is able to convert typical municipal wastes into benign and useful ingredients such as chemical byproducts or agricultural fertilizer.
- the resulting product is also capable of enzymatically catalyzing the bioremediation of chlorinated hydrocarbons and long chain hydrocarbons, particularly petroleum hydrocarbons.
- the process involved in this invention provides in-situ bioremediation in a manner not believed to have been achieved in the prior art.
- the processes have the great economic benefit of not requiring typical turning or rototilling of huge windrows of waste products as typically occurs in composting operations.
- the invention also enables bioremediation of subterranean and inaccessible contaminated soil without requiring excavation or removal of the soil to gain access to the contaminants as has been done in some instances in operations where external reactor vessels are used to convert toxic chemical compounds in the presence of microorganisms that react therewith.
- This invention provides a low cost method of producing large quantities of enzymes which are instrumental in enzymatically catalyzing the bioremediation of waste and hydrocarbon materials without the need for introduction by mechanical equipment of quantities of air or oxygen typically used to support aerobic bioremediation reactions.
- a unique property of the microbes and enzymes of the invention is that bioremediation of contaminated materials appears to be taking place using what are usually considered to be aerobic bacteria, but the aerobic bacteria are operating in what is normally considered to be an anaerobic environment. That is, there is no supply of air or oxygen to the reaction activity, but rather the nutrients, contaminants, and water react with the microbes, and enzymatic catalyzation of a reaction effectively bioremediates the contaminants. If a nutrient does happen to contain oxygen, i.e. N0 3 nitrates, it should by pointed out that the present process is not intended to be dependent on any availability of oxygen from such a nutrient.
- the present invention is able to produce a bioremediating product from the sites of conventional municipal waste disposal locations and the product material, which is useful either as a fertilizer or for ensuring bioremediation of other materials or products, has a long useful shelf life. Tests performed in using this product derived from composting operations have indicated a useful shelf life is well over one year.
- the initial biomass comprises trash, horse manure and secondary sewage sludge mixed together.
- the sludge is preferable free of oily dirt and has about 18 percent solids.
- Quicklime or flyash is added to raise the pH to 12 or above and to achieve a rapid autocatalytic heat rise in a few seconds to about 200 degrees F.
- Water is added to keep the solids in the pile at about 18 percent. This maintains the moisture content at about 82 percent which is sufficient saturation to make the aerobic bacteria react in what is essentially an anaerobic environment.
- the high thermal and alkaline conditions help to stress the bacteria so that after 24 to 36 hours the bacteria are set in their ways, i.e. the population of bacteria assumes a stable character, and are ready for the further addition to the composting pile of nutrients which cool the pile and prepare it for a one to two month period to complete the biomass reduction and biodegradation of all the organic materials in the pile.
- the pile After the first addition of nutrients the pile can be left standing for 7 to 10 days with only clear water being added as required to keep the moisture level high. After this time the pile is turned once to get the outside to the inside. Then more nutrients are added and the pile can stand idle for two more weeks. Then the pile is turned once to get the outside to the inside. Then more nutrients are added and the pile can stand idle for two more weeks. Then the pile is turned a third time and further nutrients added. Then the pile continues the enzymatically catalyzed reactions until the completion is signalled by a gradual temperature drop to about 80 to 90 degrees F. at the end of the degradation process. This temperature is one indicator of the completion of the process. Another such indicator is the presence of a fine granular or silt-like consistency of the resulting organic soil.
- the composting process of the preferred embodiment is performed generally according to the following - 13 - example:
- a compost pile mixture of trash, horse manure, secondary sewer sludge, cellulose, carbohydrates, and other typical municipal organic waste is arranged in a critical mass, i.e.
- Such a compost pile typically contains indigenous microorganisms which participate in an aerobic, thermophilic and alkalinophilic reaction which is a fundamental aspect of the present process.
- the mixture has sufficient organic and inorganic nutrients to support the temperature- raising reaction including inorganic compounds of nitrogen, phosphorus, sulfur and potassium.
- inorganic compounds of nitrogen, phosphorus, sulfur and potassium Upon reaching a temperature of 115-140 degrees F. after about 10 hours, the activity of thermophilic alkalinophilic microorganisms is increased or accelerated by the additional mixing of basic or alkalinic material such as KO, CaO (lime), NaO, MgO or flyash in sufficient quantity to increase the pH level of the initial mixture to about 12 or higher. It is desirable to wait for the temperature rise before adding the alkaline material because there is a danger of killing off desirable microbes otherwise.
- the exothermic reaction continues with a substantial increase in temperature.
- facultative organisms are forced to go aerobic.
- the reactions maintain dissolved oxygen sufficient (i. e. at least 1 ppm.) to enable survival of aerobic organisms.
- the combined high pH and high temperature is believed to kill pathogenic bacteria whereas primarily aerobic thermophilic strains of microbes, including aerobes of the genus Bacillus, and their high energy enzymes continue to be reproduced or generated.
- These surviving microorganisms and enzymes are believed to go through an evolutionary process which keeps the microbes alive and makes the final composition of living bacteria and enzymes, and co-produced amino and fatty acids, useful products.
- the primary enzymes produced during the degradation process are lipase and protease, but lignase is also produced. The exact nature of mutation or recombination which is believed to take place has not been identified.
- the temperature rise of the new mixture after pH alteration may be as high as boiling water. However the useful surviving microorganisms were found to have survived even substantially higher temperatures in the presence of some moisture.
- the surviving microorganisms were also found to survive at temperatures near the freezing temperature of water.
- the process is continued for a sufficient time, approximately 24 hrs., for the compost pile to reach a desired recycled non-contaminated condition.
- the temperature drops and the pH drops to a near-neutral level of 7-7.5.
- the microorganisms can continue to multiply in the presence of moisture and nutrients and the end product includes high energy enzymes with improved cleavage ability for bioremediation of hydrocarbon contaminants from soil and the resulting production of innocuous water and C0 2 .
- the combined waste materials and additives are solids which facilitates handling the materials.
- Metal ions in the reacting mixture do not impede the formation of useful enzymes which are retrievable as useful products for bioremediation of hydrocarbons and for regenerating biofouled activated carbon used in other processes.
- the trash and horse manure can be added to the composting mixture after the stressing period.
- the horse manure is added first so that the bacteria therein are subjected to the high temperature and high pH before the addition of trash which has a high paper content tending to bring the pH down rapidly.
- Another such indicator is the presence of fine granular or silt-like consistency of the resulting organic soil.
- the molecular structure of the microbes and their enzymes resulting from the processing steps of the present invention are not specifically known, it is recognized that these microbes and their enzymes have been subject to extremes of temperature and pH during the aerobic metabolic process taking place. For at least a short time of the order of 24 hours the microbial products are very highly stressed and it is believed that only the highly thermophilic microbes survive. It is believed that not only are pathogenic microbes killed or permanently denatured by the heating, but also it is believed that even those of the thermophilic microbes which may be denatured at temperatures of the order of 100 degrees C. may be renatured during the cooling achieved after about 48 hours upon the addition of the nutrients. After nutrient addition not only does the temperature drop but also the pH also drops from somewhere in the vicinity of 12-14 pH to around 7-8 pH.
- the Similarity and Distance Coefficient for each strain shown in Table 3 refers to the similarity and distance to the hypothetical "mean" organism in the database.
- the database organism has a similarity coefficient of one and a distance of zero. The closer a strain is to respective coefficients of one and zero, the more closely it matches the means organism of the database. A good match is one with a similarity coefficient greater than 0.5 and a distance coefficient of less than 7.
- Table 4 shows the growth rate of aerobic and anaerobic bacteria of the invention:
- Bioremediation and Fertilizers A secondary aspect of the present process is to mix a concentrated portion of the solid material produced by the above process and containing surviving living or active organisms with water and use the liquid mixture to inoculate and bioremediate soil contaminated with hydrocarbons (as from fuel spills or tank leakage) and chlorinated hydrocarbons (pesticides, PCBs, etc.).
- the percentage of gypsum in the final composted product can be varied over a range of about 3 to 12 percent by varying the quantity of nutrients added.
- Phosphogypsum will also be present in a significant amount and its relative degree of presence can be varied by changes in the relative amount of (0-45-0) super triple phosphate which is used.
- Bioremediation As pointed out above, the composting end product from the preferred composting process may, in lieu of use as an organic fertilizer, be used for bioremediation of various organic and hydrocarbon substrate materials.
- the generation and recovery of useful products such as amino and fatty acids provides a significant economic benefit derived from these processes.
- An additional important feature of the present invention is that the bacteria achieved by the initial composting operation are not selective, i.e., they can be made to bioremediate a large variety of different hazardous or contaminating materials and thus provide a more inclusive process of generic application without the necessity of extensive analytical preparation to determine the location of contaminants, the type of bacteria needed to bioremediate the contaminants and an expectation that most contaminants can be treated by the products of this invention to break them down to benign or innocuous materials such as water and carbon dioxide and potentially beneficial acids.
- the nutrients added for such a subsequent process are preferably (46-0-0) urea, (32-0-0) ammonium nitrate, (0-45-0) phosphate and (0-0-30) potash with the nitrogens being 10 to 1 by weight relative to the total phosphorus and potassium.
- Such a subsequent process may be of the type shown and described in connection with FIGS. 5-7 and 9-10.
- the moisture content can drop as low as about 20 percent by weight and still preserve the necessary conditions for an enzymatically catalyzed bioreaction.
- Another embodiment of the invention involves the bioremediation of paraffin crude oil in a mixture of other composting materials.
- This paraffin crude is typically in an earthen pit and is mixed with water.
- secondary digester sludge having about 3 to 5 percent moisture by weight is mixed with horse manure in a pile using the sludge as the wetting agent. After mixing, the overall moisture in the pile reduces to about 50 percent by weight.
- whole trash mainly paper products such as magazines, cardboard boxes, paperback books and newspapers are added to the pit to absorb the crude oil and water forming an oily trash mix with a resulting average hydrocarbon content of 30 percent (300,000 ppm.) Total Petroleum Hydrocarbons (TPH) per the 418.1 Infrared
- the amounts of the mix ingredients are 110 yds. (cu. yds.) horse manure, 2000 gals, sludge, 50 yds. trash and 25 yds. of the paraffin crude oil.
- the pile may be turned at that time mainly to get outside layers to the inside of the pile. Under the same type of high moisture content of at least 60 to 75 percent the overall mixture is biodegraded with the hydrocarbons being bioremediated by a continuing enzymatically catalyzed microbial action. After 30 days the pile temperature levels off at about 130 degrees F. and the pile is turned once more, again just to get the outside to the inside for better action. At this time the TPH is down to 2000 to 3000 ppm. After 60 to 90 days the TPH levels dropped to less than 100 ppm. which is acceptable as a level of satisfactory bioremediation of the hydrocarbons.
- Another embodiment of the invention relates to the use of an aerobic microbial product for bioremediation of subsurface or underground contaminants such as spills or seepage in the vicinity of buried storage tanks, as typically used for storage of gasoline or other liquid products which are deemed hazardous contaminants due to their ability to migrate through soil or other ground materials and mix with and contaminate ground water to make the latter non-potable, or at least less useful.
- the present invention contemplates assuring bioremediation at such sites is successfully and expediently performed by assuring the presence of suitable microbes and enzymes with needed nutrients and enough water moisture to enable aerobic reaction of the microbial product with nutrients and the contaminating substrate which is to be converted to benign products.
- this embodiment of the invention contemplates the use of at least two spaced vertically extending wells or bore holes of small diameter extending to a depth at least equal to the depth of the deepest layer portion of any contaminated substrate layer. Referring to FIG.
- subsurface bioremediation system 10 is installed in earth 12 having surface 14 and contaminated area 16 located at a depth of from about five feet to about ten feet below surface 14.
- Positively charged well 18 is vertically disposed, extending from surface 14 downwardly through contaminated area 16, in the instant case for a total of about ten feet.
- Well liner 20 extends the length of well 18, fitting against the inside surface of the borehole thereof, well liner 18 having at its lower end an endcap 22.
- Well liner 20 has perforations 24 located along its lower portion within the area of contaminated area 16, i.e., the lower five feet thereof.
- Well liner 20 may be constructed from polyvinyl chloride (PVC) pipe. Perforations 24 are of about
- PVC polyvinyl chloride
- the perforated portion of the PVC pipe may be conventional well monitoring PVC pipe having multiple small arcuate circumferentially extending slits along the length of the perforated pipe portion.
- Positively charged coaxial electrode 26 is located within well 18, concentric with well liner 20 and extending substantially the entire length thereof, the lowermost five feet of electrode 26 being in communication with contaminated earth 16 by means of perforations 24 in well liner 20.
- Coaxial electrode 26 is formed of from 3//4 to 1 inch diameter standard copper tubing and is perforated with apertures 28 of approximately 1/8 in. diameter at 3 inch intervals over the portion of the length of electrode 26 corresponding to the perforated portion of well liner 20-, preferably for a minimum of 2 feet of the perforated portion of liner 20.
- Electrode 26 is positively charged through its connection with DC electric generator 30 by means of wire 32.
- Negatively charged well 34 is spaced from positively charged well 18 and is preferably located at a location extending into a portion of contaminated area 16 remote from positively charged well 18. Negatively charged well 34 may be identical in configuration to positively charged well 18.
- Well 34 comprises well liner 36 having end cap 38, the lower five feet thereof having perforations 40 extending therealong.
- Negatively charged concentric electrode 42 may be identical in configuration to positively charged electrode 26, and is located within well 34, extending substantially the entire length thereof, the lowermost five feet of electrode 42 being in communication with contaminated earth 16 by means of perforations 40 in well liner 36.
- Electrode 42 is constructed of standard copper tubing in a similar manner to electrode 26 and is perforated with apertures 44 similarly disposed as apertures 28 in electrode 26.
- Electrode 42 is negatively charged by means of its connection with DC generator 30 by means of wire 46.
- the upper portion of negatively charged electrode 42 is connected with tank 48 by means of hose 50 for fluid flow between tank 48 and electrode 42.
- FIG. 6 is an expanded view of negatively charged well 34, negatively charged electrode 42, and its connection with hose 50.
- FIG. 7a is a plan view of a typical layout of wells as in FIG. 5 for a circularly disposed contamination area 16, wherein negatively charged well 34 is located in the center of the contamination area 16 and a plurality of equally spaced positively charged electrodes are located near the perimeter of the contamination area 16 and equidistant from centrally located negatively charged well 18.
- the relative charges may be reversed, it is most convenient to provide liquid from tank 48 (See FIG. 5) to a single negative electrode. In the illustrated case, six well pairs are formed by six positively charged wells 18 and a single negatively charged well 34.
- FIG. 7b is a plan view of a typical layout of wells as in FIG. 5 for a rectangularly disposed contamination area 16, wherein a plurality of negatively charged well 34 are located along one side of contaminated area 16 and a corresponding number of positively charged wells 18 are located along the opposite side of contamination area 16. In the illustrated case, three well pairs are formed by three positively charged wells 18 and three negatively charged wells 34.
- nutrients, microbes and water to support subsurface bioremediation are supplied in selectively controlled amounts by gravity to negatively charged wells 34 by hose 50 from a tank 48 located on surface 14. Sufficient water is added to the wells to assure ability of bacteria to migrate in the earth material if the contaminants are not below the water table level. Water containing a few ounces of aerobic bacteria and nutrients including nitrates or urea and phosphates is fed by gravity into the bore hole through the hollow negative electrode, which is perforated with apertures 44.
- the electrodes are energized for several hours to stimulate or stress the microbes and to deliver the microbes and enzymes and nutrients horizontally throughout the contaminated area to act upon the nutrients to perform an enzymatically catalyzed hydrolysis of the substrate in the presence of the water to provide availability of sufficient oxygen for a continuing aerobic bioremediation action on the contaminants even after the power from the welder is interrupted.
- the enzymatically catalyzed hydrolysis of the substrate in the presence of water and the microbial action on the nutrients can continue under aerobic conditions without having to aerate or otherwise supply oxygen to the contaminated mass.
- These hydrolysis reactions in the presence of water continue long after the electrical energization of the water from the electrodes has been discontinued.
- the negative electrode In another test across an electrode spacing of about 430 feet, 80 gallons of nutrient rich solution were fed to the negative electrode to a nutrient deficient contaminated mass of earth at a depth of 7 to 12 feet, the negative electrode being shielded for the first 7 feet and exposed to the contaminated 5 foot layer by means of perforations in the PVC pipe. Between two vertical electrodes of opposite polarity, the DC electric field as seen from above would be oval or like a football in shape. When using multiple electrodes these shapes can be made to overlap in any desired field pattern.
- One or more negative electrodes can be located at the center of a circular area, as in FIG. 7a, or along one side of a grid or network pattern, as in
- FIG. 7b to define a horizontally extending area having one or more DC electric field patterns.
- Ex-Situ Bioremediation of Liquid Wastes In addition to the in-situ bioremediation process just described where the remaining degraded constituents may typically be left in place, it is also possible to utilize techniques of this invention to perform ex-situ processing, i.e., moving a quantity of liquid waste or contaminated solid material or soil into a container for bioremediation.
- the bioremediating product is believed to be suitable for bioremediation of categories of contaminants as follows:
- a process for such treatment in accordance with one embodiment of the invention may be performed in an inert plastic 55 gallon drum of PVC material (see FIG. 10) for action on liquid substrates such as hydrocarbons.
- the drum is placed on end and filled to within about 10-12 inches of the open top with sand.
- About 5 to 15 gallons of the substrate liquid is mixed with the sand to coat the surface of the sand particles.
- Clear water is added to fill the barrel to a level a few inches above the sand/waste mix and a small quantity of aerobic seed microbes and a quantity of nutrients are added.
- the color of the water in the top of the drum is a visual indicating means to verify when the remediation process is complete. When the water color turns dark, indicating such completion, the liquid is removed from the drum except for about 6 inches in the bottom which serves as microbe seeding for additional processing.
- the remediated waste may be removed by means of a manually or remotely controlled drain valve at the periphery of the lower end of the drum. Separate drain valves can be used to facilitate on the one hand keeping a 6 inch level of substrate in the container for seeding, and on the other hand allowing complete removal of the remediated substrate.
- bioremediation operations can be performed at regular intervals. This process lends itself to use in a manufacturing plant or the like where hazardous waste is being generated continuously as part of a continuing manufacturing or industrial operation.
- the substrate to be bioremediated is a particular material, it is likely to be the case that one or more particular amino acid or fatty acid byproducts will be produced by enzymatic action on the substrate.
- the products drained from the drum after a processing operation may subsequently be passed through a separating process to isolate any desired amino acid or fatty acid product.
- Such products usually have a significant market value and their sale may constitute a significant recycling step and help reduce the cost of disposal of hazardous waste.
- bioremediation by-products produced when using the present invention are fatty acids which are produced as a result of microbial action on the hydrocarbons and amino acids which are probably produced mostly as a result of the breakdown or death (lysis) of the microbes. It is apparent that there may be some real commercial potential in recovering fatty acids as remediation co-products. They are much more concentrated; they are present at a percent or so of the sample weight.
- the contaminated material may be added to the reactor without or mixed with sand or other solid media.
- the bioremediated solid material must then be periodically removed from the reactor.
- An example of the bioremediation of contaminated soil is discussed below.
- the process of this invention has been applied to a pit (see FIG. 9) measuring about 12 feet by 18 feet by 2 feet deep with a beginning total petroleum hydrocarbon level in the soil forming the pit of about 20 percent.
- a centrally located vetical tube is installed in the pit and extends into the earth below the pit to extract bioremediation products.
- the treatment was begun by forming a pond by adding about 40 barrels of water to the pit plus fertilizer plus about 10 ounces of the compost end product of this invention. Every few days, a dark-colored water was removed from the pit and then more clear water and fertilizer or nutrient were added.
- Threonine 2.12 mg/100 gm
- Palmitoleate C l6 l 1.33
- compost-produced bioremediation product of this invention is believed to be non-specific as to the substrates which can be treated and bioremediated thereby.
- any byproducts produced by such remediation process will be substrate specific, i.e. the byproduct will depend on the composition of the substrate being broken down.
- An example of production of an amino acid from a hazardous waste is the production of tyrosine from biodegradation of toxaphene-contaminated soil using microbial products of the present invention.
- Toxaphene is one of the compounds highly resistant to biological attack because of its high chlorine content, nearly 70 percent chlorine. See FIG. 8 for an illustration of a tank useful for bioremediating toxaphene-contaminated soil. The process steps employed are similar to those used in the ex-situ bioremediation of wastes described above. Clear water is added to the tank to a desired level (about 3 inches) above the contaminated soil. A small quantity of aerobic seed microbes obtained from the composting process of this invention and a quantity of nutrients are added.
- a hydrolysis reaction may be catalyzed abiotically or biotically.
- Several sources confirm that hydrolysis proceeds faster when mediated by microbes.
- Enzymatic hydrolysis is expedited when enzymes hold reacting species in the "right positions" enhancing rates of interaction. By doing this, unfavorable changes in energies of activation are avoided.
- These compound-enzyme complexes are subsequently separated by attack with water. The end result is as if a direct attack on the complexes was performed exclusively by water.
- Enzymatic hydrolysis is believed to be a major degradation mechanism used in the present process for treatment of contaminated soils.
- the enzymatic nature of the culture increases the rates of degradation and lowers substrate specificity of treatment.
- technologies such as air sparging (blowing air in) and soil vapor extraction (replacing with fresh air) may well become obsolete.
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- Biotechnology (AREA)
- Biochemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- General Health & Medical Sciences (AREA)
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Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EA199700229A EA000660B1 (en) | 1995-03-13 | 1996-03-13 | Biomass reduction and bioremediation processes and products |
EP96911348A EP0817763A4 (en) | 1995-03-13 | 1996-03-13 | Biomass reduction and bioremediation processes and products |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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US40271195A | 1995-03-13 | 1995-03-13 | |
US08/402,711 | 1995-03-13 |
Publications (1)
Publication Number | Publication Date |
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WO1996028400A1 true WO1996028400A1 (en) | 1996-09-19 |
Family
ID=23593018
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/US1996/003775 WO1996028400A1 (en) | 1995-03-13 | 1996-03-13 | Biomass reduction and bioremediation processes and products |
Country Status (3)
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---|---|
EP (1) | EP0817763A4 (en) |
EA (1) | EA000660B1 (en) |
WO (1) | WO1996028400A1 (en) |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL1007712C2 (en) * | 1997-12-05 | 1999-06-08 | Biosoil B V | In-situ method for cleaning a bottom portion contaminated with halogenated products, especially chlorinated products. |
FR2826884A1 (en) * | 2001-07-04 | 2003-01-10 | Philippe Brisset | Method of treating household, catering and industrial organic waste and dredging muds by first treating biologically in highly aerated conditions and then chemically |
WO2003004442A3 (en) * | 2001-07-04 | 2003-11-06 | Naturem Environnement | Method for treating waste, devices and compositions for carrying out said method |
US6878179B2 (en) * | 2001-12-31 | 2005-04-12 | Microbes, Inc. | Fertilizer compositions and methods of making and using same |
EP2138245A1 (en) * | 2008-06-26 | 2009-12-30 | Biodermol S.r.l. | Process for decontaminating soils polluted by at least one pollutant among hydrocarbons, dioxin and phenols |
WO2012115589A1 (en) * | 2011-02-25 | 2012-08-30 | Telge Nät Ab | Method and system for sanitization of pathogen containing liquid waste in composting applications |
CN103691737A (en) * | 2014-01-09 | 2014-04-02 | 江苏麦可博生物环保工程技术有限公司 | Combined process for ex-situ remediation of degradation-resistant organic contaminated soil by microorganisms |
RU2516468C2 (en) * | 2012-06-22 | 2014-05-20 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Кубанский государственный аграрный университет" | Method of reclamation of agricultural lands |
RU2516454C2 (en) * | 2012-06-22 | 2014-05-20 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Кубанский государственный аграрный университет" | Method of obtaining organic-mineral compost |
RU2536457C1 (en) * | 2013-07-15 | 2014-12-27 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Кубанский государственный аграрный университет" | Method of improvement of soil fertility |
ES2555358A1 (en) * | 2015-03-03 | 2015-12-30 | Acciona Agua, S.A.U. | Biological pretreatment method for hydrolysis processes (Machine-translation by Google Translate, not legally binding) |
CN106925598A (en) * | 2017-03-08 | 2017-07-07 | 上海应用技术大学 | A kind of garbage degradation sorting arrangement and garbage degradation method for sorting |
WO2018236340A1 (en) * | 2017-06-19 | 2018-12-27 | Mast David Jay | An organic waste treatment process and device |
US10190769B2 (en) | 2010-08-19 | 2019-01-29 | Newfoss Holding B.V. | Process for the conversion of biomass of plant origin, and a combustion process |
US11104850B2 (en) | 2017-09-07 | 2021-08-31 | Mcfinney, Llc | Methods for biological processing of hydrocarbon-containing substances and system for realization thereof |
Families Citing this family (2)
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MD4144C1 (en) * | 2011-09-22 | 2012-07-31 | ГЛАВНЕНКО Николае | Process for waste-free production from humus-containing substances of a fertilizer and a biostimulant for growth and development of plants |
CN111170790A (en) * | 2020-02-11 | 2020-05-19 | 刘文治 | Method for preparing water-soluble liquid fertilizer from household classified kitchen waste |
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US5466273A (en) * | 1994-04-28 | 1995-11-14 | Connell; Larry V. | Method of treating organic material |
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JP3252246B2 (en) * | 1993-03-09 | 2002-02-04 | 木村 美津代 | Fermented products and their manufacturing method |
EP0745573A4 (en) * | 1994-12-20 | 1998-10-21 | Mitsuyo Kimura | Fermentation product and process for producing the same |
-
1996
- 1996-03-13 EA EA199700229A patent/EA000660B1/en not_active IP Right Cessation
- 1996-03-13 WO PCT/US1996/003775 patent/WO1996028400A1/en not_active Application Discontinuation
- 1996-03-13 EP EP96911348A patent/EP0817763A4/en not_active Withdrawn
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US4743287A (en) * | 1984-09-24 | 1988-05-10 | Robinson Elmo C | Fertilizer and method |
US5169782A (en) * | 1991-02-12 | 1992-12-08 | Rey Tech, Inc. | Apparatus and method for processing organic refuse |
US5466273A (en) * | 1994-04-28 | 1995-11-14 | Connell; Larry V. | Method of treating organic material |
Non-Patent Citations (1)
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See also references of EP0817763A4 * |
Cited By (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0924000A1 (en) * | 1997-12-05 | 1999-06-23 | Biosoil B.V. | In-situ method for cleaning a soil fraction contaminated with halogenated products, particularly chlorinated products |
US6175052B1 (en) | 1997-12-05 | 2001-01-16 | Biosoil B.V. | In-situ method for cleaning soil polluted with halogenated products |
NL1007712C2 (en) * | 1997-12-05 | 1999-06-08 | Biosoil B V | In-situ method for cleaning a bottom portion contaminated with halogenated products, especially chlorinated products. |
FR2826884A1 (en) * | 2001-07-04 | 2003-01-10 | Philippe Brisset | Method of treating household, catering and industrial organic waste and dredging muds by first treating biologically in highly aerated conditions and then chemically |
WO2003004442A3 (en) * | 2001-07-04 | 2003-11-06 | Naturem Environnement | Method for treating waste, devices and compositions for carrying out said method |
US6878179B2 (en) * | 2001-12-31 | 2005-04-12 | Microbes, Inc. | Fertilizer compositions and methods of making and using same |
US7044994B2 (en) | 2001-12-31 | 2006-05-16 | Microbes, Inc. | Fertilizer compositions and methods of making and using same |
US7442224B2 (en) | 2001-12-31 | 2008-10-28 | Microbes, Inc. | Fertilizer compositions and methods of making and using same |
EP2138245A1 (en) * | 2008-06-26 | 2009-12-30 | Biodermol S.r.l. | Process for decontaminating soils polluted by at least one pollutant among hydrocarbons, dioxin and phenols |
US10190769B2 (en) | 2010-08-19 | 2019-01-29 | Newfoss Holding B.V. | Process for the conversion of biomass of plant origin, and a combustion process |
US10982849B2 (en) | 2010-08-19 | 2021-04-20 | Newfoss Holding B.V. | Process for the conversion of biomass of plant origin, and a combustion process |
WO2012115587A1 (en) | 2011-02-25 | 2012-08-30 | Delaval Holding Ab | Method and system for the sanitization of a digestate in the production of biogas |
WO2012115589A1 (en) * | 2011-02-25 | 2012-08-30 | Telge Nät Ab | Method and system for sanitization of pathogen containing liquid waste in composting applications |
RU2516468C2 (en) * | 2012-06-22 | 2014-05-20 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Кубанский государственный аграрный университет" | Method of reclamation of agricultural lands |
RU2516454C2 (en) * | 2012-06-22 | 2014-05-20 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Кубанский государственный аграрный университет" | Method of obtaining organic-mineral compost |
RU2536457C1 (en) * | 2013-07-15 | 2014-12-27 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Кубанский государственный аграрный университет" | Method of improvement of soil fertility |
CN103691737A (en) * | 2014-01-09 | 2014-04-02 | 江苏麦可博生物环保工程技术有限公司 | Combined process for ex-situ remediation of degradation-resistant organic contaminated soil by microorganisms |
ES2555358A1 (en) * | 2015-03-03 | 2015-12-30 | Acciona Agua, S.A.U. | Biological pretreatment method for hydrolysis processes (Machine-translation by Google Translate, not legally binding) |
CN106925598A (en) * | 2017-03-08 | 2017-07-07 | 上海应用技术大学 | A kind of garbage degradation sorting arrangement and garbage degradation method for sorting |
WO2018236340A1 (en) * | 2017-06-19 | 2018-12-27 | Mast David Jay | An organic waste treatment process and device |
US11104850B2 (en) | 2017-09-07 | 2021-08-31 | Mcfinney, Llc | Methods for biological processing of hydrocarbon-containing substances and system for realization thereof |
US11655420B2 (en) | 2017-09-07 | 2023-05-23 | Mcfinney, Llc | Methods for biological processing of hydrocarbon-containing substances and system for realization thereof |
Also Published As
Publication number | Publication date |
---|---|
EP0817763A4 (en) | 2000-05-31 |
EA199700229A1 (en) | 1998-02-26 |
EA000660B1 (en) | 1999-12-29 |
EP0817763A1 (en) | 1998-01-14 |
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