AU2901689A – Microorganism for use in industrial processes
– Google Patents
AU2901689A – Microorganism for use in industrial processes
– Google Patents
Microorganism for use in industrial processes
Info
Publication number
AU2901689A
AU2901689A
AU29016/89A
AU2901689A
AU2901689A
AU 2901689 A
AU2901689 A
AU 2901689A
AU 29016/89 A
AU29016/89 A
AU 29016/89A
AU 2901689 A
AU2901689 A
AU 2901689A
AU 2901689 A
AU2901689 A
AU 2901689A
Authority
AU
Australia
Prior art keywords
ferroxifunis
bagdadii
microorganism
growth
iron
Prior art date
1987-12-10
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
AU29016/89A
Inventor
James Waskovsky
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chemolithotrophs Inc
Original Assignee
Chemolithotrophs Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
1987-12-10
Filing date
1988-12-12
Publication date
1989-07-05
1988-12-12
Application filed by Chemolithotrophs Inc
filed
Critical
Chemolithotrophs Inc
1989-07-05
Publication of AU2901689A
publication
Critical
patent/AU2901689A/en
Status
Granted
legal-status
Critical
Current
Links
Espacenet
Global Dossier
Discuss
Classifications
C—CHEMISTRY; METALLURGY
C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
C02F3/00—Biological treatment of water, waste water, or sewage
C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
C02F3/345—Biological treatment of water, waste water, or sewage characterised by the microorganisms used for biological oxidation or reduction of sulfur compounds
C—CHEMISTRY; METALLURGY
C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
C10L9/00—Treating solid fuels to improve their combustion
C—CHEMISTRY; METALLURGY
C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
C—CHEMISTRY; METALLURGY
C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
C22B3/18—Extraction of metal compounds from ores or concentrates by wet processes with the aid of microorganisms or enzymes, e.g. bacteria or algae
C—CHEMISTRY; METALLURGY
C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
C12R—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C – C12Q, RELATING TO MICROORGANISMS
C12R2001/00—Microorganisms ; Processes using microorganisms
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
Y02P10/00—Technologies related to metal processing
Y02P10/20—Recycling
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
Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
Y10S435/00—Chemistry: molecular biology and microbiology
Y10S435/8215—Microorganisms
Y10S435/822—Microorganisms using bacteria or actinomycetales
Description
MICROORGANISM FOR USE IN INDUSTRIAL PROCESSES BACKGROUND OF THE INVENTION
Field Of The Invention
This invention relates to a novel microorganism, Ferroxifunis bagdadii, and its isolation and purification from a natural source. This invention also relates to industrial processes utilizing a pure culture of Ferroxifunis bagdadii, including the bioextraction of mining ores and tailings, the degradation of textile plant wastewater pollutants into innocuous materials compatible with the environment, and the liquefaction and desulfurization of coal.
Brief Desc ript ion Of The Prior Art
Bioextraction Of Mining Ores: Microorganisms have been used to leach o res from mine waters for about thirty years. The basic reaction mediated by microorganisms is:
4FeSO4 + 2H2SO4 + O2 (electron receptor) → 2Fe2(SO4)3 + 2H2O.
Ferric iron is required to oxidize the sulfide in the minerals, thereby releasing copper into the acidified solution. Thiobacillus ferroxidans is one microorganism with known utility in this regard. T. ferroxidans exhibits an iron oxidation rate of 40-50 mg/1/hour for 106 bacterie/cm3. However, there are many characteristics of Thiobacillus which
limit its bioextractive utility. Among other things,
Thiobacill i exhibit a slow growth rate and are intolerant of light, arsenic, chlorides, high copper content, high temperatures, lack of oxygen, and high molybdenum-concentrations. Attempts to overcome the growth rate problem. and increase the iron oxidation rate observed with Thiobacillus have included the addition of silver to the effluent, which increases the iron oxidation rate to 360 mg/1/hour.
Degradation Of Textile Plant Wastewater Pollutants: Inherent in the manufacturing of textiles is the production of wastewater containing organic and inorganic materials which render the wastewater unsuitable for reuse and/or release into the biosphere.
Known processes for degrading textile plant wastewater pollutants have incorporated the utilization of microorganisms such as Thiobacillus. However, such organisms do not survive well in industrial effluents containing starches, formaldehyes and alcohols, thus limiting their utility in degrading wastewater pollutants.
Desulfurization Of Coal: In recent years, the problem of «acid rain» has become well-known. The problem originates in the burning of coal to which sulfur is bound. Upon combustion, sulfur dioxide (SO2) is released into the atmosphere where it will combine with rain water to form sulfuric acid, hence, the term «acid rain.» Present methods of dealing with the problem of desulfurizing coal have included
the utilization of microorganisms such as Thiobacillus thioparus. However, the slow growth of Thiobacillus requires several weeks residence time in the bioreactor. In addition,
Thiobacillus requires aerobic, acidophillic and autotrophic conditions for growth.
SUMMARY OF THE INVENTION
Accordingly, it is an object of this invention to provide a biological process for the extraction of metal ores from dump ores or mine tailings utilizing a microorganism which grows well and exhibits a high iron oxidation rate in mine effluent. A further object of this invention is to provide a biological process for the extraction of metal ores utilizing a culture of the microorganism Ferroxifunis bagdadii.
Another object of this invention is to provide a biological process for the treatment of textile mill wastewater effluent utilizing a microorganism which can survive in wastewater containing products such as starches, formaldehydes, and alcohols; can turn pollutants into innocuous materials compatible with the environment; and which, because of its sulfur oxidizing abilities, can oxidize diazo dyes to the standards of the Environmental Protection Agency (EPA). A further object of this invention is to provide a process for the biological degradation of textile plant wastewater pollutants utilizing a pure culture of the microorganism Ferroxifunis bagdadii.
Yet another object of this invention is to provide a biological process for desulfurizing coal, prior to combustion, utilizing a microorganism that grows quickly enough to limit residence time in bioreactors to a matter of days and whose growth is not dependent on the presence of aerobic, acidophilic, mesophilic, and autotrophic conditions. A further object of this invention is to provide a process for desulfurizing coal, prior to combustion, utilizing a pure culture of Ferroxifunis bagdadii.
An additional object of this invention is to provide a pure culture of Ferroxifunis bagdadii.
In one embodiment, this invention provides a process for the extraction of metal ores from dump ores or mine tailings, which comprises treating effluent and/or mine heaps with a pure culture of the microorganism Ferroxifunis bagdadii.
In another embodiment, this invention provides a process for degrading textile mill wastewater which comprises treating wastewater effluent from a textile mill with a pure culture of the microorganism Ferroxifunis bagdadii.
In another embodiment, this invention provides a process for desulfurizing coal, prior to combustion, which comprises innoculating coal with a pure culture of the microorganism Ferroxifunis bagdadii.
In yet another embodiment , this invention provides a pure culture of the microorganism Ferroxifunis bagdadii, having the characteristics described below.
DETAILED DESCRIPTION OF THE INVENTION
The microorganism Ferroxifunis bagdadii was isolated from acid mine effluent at the Cyprus Bagdad Company located in
Bagdad Arizona.
The pure culture was isolated from 200 cc undiluted mine effluent to which various supplements were added. After incubation at 37 °C for four days, a rusty coloration was observed in the effluent to which had been added: 0.1 gram ascorbic acid, 0.1 g MgSO4 7H2O, 0.02g Na-molybdenate, and
5.6 grams FeSO4; henceforth, referred to as the isolating medium.
Ten milliliter aliquouts of isolating medium were then added to 100 milliliters of solutions containing arsenic (5 ml. of 1.5% arsenic trioxide solution), copper (5 g/l CuSO4), molybdenum (0.3 g/l sodium molybdenate), 5 ml concentrated xylene, zinc (5 g/l ZnSO4). The basic solution contained 0.4 g/l K2HPO4, 0.4 g/l (NH4)2SO4, and 0.4 g/l MgSO4
7H2O. All solutions were incubated at 37 °C. Growth, as judged by turbidity, was observed within 72 hours. Further purification was carried out with an inoculant from the copper-containing solution.
A 5 ml inoculant from the copper-containing solution was placed in 100 ml. of the basic solution described above which additionally contained either 10, 20, or 30 g/l CuSO4
All solutions were incubated at 37 °C. Growth, as judged by turbidity, was noted within four days, in tubes containing 10
and 20 g/l CuSO4. No growth was observed in the solution containing 30 g/1 CuSO4.
For further purification, inocula were taken from the solution containing 20 g/l CuSO4 and streaked, with a wire loop, on solid agar-agar media containing basal salts (0.4 g K2HPO4, 0.4 g (NH4)2SO4 and 0.4 g MgSO4 7H2O), and 10, 20 or 30 g/1 CuSO4.
Distinct colonies were observed after four days incubation at 37 °C and the addition of gram stain revealed the presence of gram negative rods. An isolated colony from the plate containing 20 g/l CuSO4 was streaked onto a similar plate. Colony growth was observed after six days incubation at 37 °C. Again, the addition of gram stain revealed the presence of gram negative rods. The procedure was repeated three times to obtain pure colonies. Purity was confirmed with scanning electron microscopy.
Pure cultures were maintained in liquid feedstock containing 0.4 g/l K2HPO4, 0.4 g/l (NH4)2SO4, 0.4 g/l MgSO4 7H2O, 27 . 8 g/l FeSO4 7H2O, and 10 ml. Bagdad mine effluent. Pure cultures were also maintained on slants containing an agar-agar/basal salt solid medium prepared as follows: Basal salts (0.4 g (NH4)2SO4, 0.4 g MgSO4 7H2O, 0.4 g K2HPO4) were added to 500 ml distilled water. This solution was acidified with concentrated sulfuric acid to pH 2.1. In a second flask, 12 grams agar-agar was added to 500 ml distilled water. Both flasks were subjected to 15 PSI at 126 °C for 20 minutes. After cooling to 40 °C,
the contents of both flasks were combined in a third flask to which was added 27.8 g FeSO4.
The pure Ferroxifunis bagdadii is a weakly gram negative, non-spore forming, double stranded rope-like organism with a possible polar appendage. Figure 1 is an electron micrograph showing the double stranded, rope-like appearance of the Ferroxifunis at 18,000 magnification. The cells are about
4 microns in length and 0.25 microns in width and are free swimmers. Ferroxifunis bagdadii is a facultative anaerobe, exhibiting good growth in a CO2 enriched environment. The cells form large spreading colonies on heterot rophic media. No vitamin supplements are required for growth. No odor is given off by cultures of Ferroxifunis bagdadii on inorganic media while a pungent odor is given off by cultures on nutrient broth. With the passage of growth time on organic media,
Ferroxifunis bagdadii forms a pellical on the surface of a narrow mouth tube.
Ferroxifunis bagdadii forms transparent, concave, pinpoint colonies with a smooth edge on solid media containing silver and copper. Brown-orange encrustations are observed when growth occurs on iron media. Growth in the presence of aluminum, iron or ammonium leads to the formation of jarosite.
Peach fuzz growth is observed on media containing basal salts.
Ferroxifunis bagdadii is very tolerant of heavy metals, such as arsenic, copper, antimony, silver, uranium, iron, and molybdenum. The microorganism is a strong iron oxidizer. Iron
oxidation rates in excess of 900 mg/1/hour have been observed in straight mine effluent. The ferrous iron content of copper mine effluents vary but even at iron concentrations of 28 g/l,
Ferroxifunis oxidizes ferrous iron to ferric iron. The pH of copper mine effluents typically runs between 1.5 and 3.0 and
Ferroxifunis will oxidize iron in this range. The microorganism will also oxidize iron over a wide range of temperatures, as shown in Figure 2. At 5 °C, an iron oxidation rate of 600 mg/l/hour is observed; at 37 °C, 1000 mg/l/hour.
Ferroxifunis bagdadii can also derive energy f rom the oxidation of sulfur, sulfide, sulfite, thiosulfates, polythionates, antimony and carbon. Furthermore, the microorganism grows well in toxic solutions (1 g/l) of thioacetamide.
Ferroxifunis bagdadii is also capable of decolorizing textile wastewater. Unlike other microorganisms used for this purpose, Ferroxifunis does not require constant pH monitoring, a continuous food supply, or a large amount of substrate to maintain activity. In addition, Ferroxifuni s is not easily shocked by large loadings. Furthermore, Ferroxifunis survives well in industrial solvents such as formaldehydes and alcohols.
A suitable growth temperature range for Ferroxifunis bagdadii is about 5° to 40°C, with optimal growth occurring at 37°C. The microorganism is also thermoduric, surviving at temperatures as high as 80 °C. A suitable pH range is 1.7 to
9.4, with optimal growth occurring at pH 2.1 on inorganic media and at pH 3.8 on organic media.
On the basis of the morphological, cultural, and physiological characteristics set forth above, it has been determined that this microorganism is a new species, designated as Ferroxifunis bagdadii. A culture of this strain has been deposited in the American Type Culture Collection and has received an accession number, ATCC-53601.
The microorganism Ferroxifunis bagdadii can be employed alone or in combination with other microorganisms conventionally used in the described industrial processes. This invention also includes the use of any variants of Ferroxifunis bagdadii either alone, or in combination with other conventionally used microorganisms.
In order to further demonstrate the effectiveness of the pure culture of Ferroxifunis bagdadii, the following examples are given as exemplary of the invention but without intending to limit the invention to these examples.
EXAMPLE 1 – BIOEXTRACTION OF ORES
Experimentation was performed to release copper from chalcopyrite, CuFeS2 according to the following reaction mediated by Ferroxifunis bagdadii:
CuFeS2 + 6 H2SO4 → CuSO4 + FeSO4 +
5 SO2 + 6 H2O + S
Cha lcopyr i te (1500 grams) was washed in tap water and placed in a one gallon jar. Basal salts (0.75 g/l MgSO4,
EXAMPLE 3 – DESULFURIZATION OF COAL
Experimentation was performed to demonstrate the effectiveness of Ferroxifunis in desulfurizing coal.
Coal of U.S. Standard Sieve -60 mesh, containing 2.8% sulfur was added to 3 liters distilled water. This 14% coal slurry was acidified with concentrated sulfuric acid to a pH of 4.2. Basal salts 1.5 g MgSO4, 1.5 g (NH4)2SO4, 1.5 g K2HPO4) and sucrose (15 grams) were added to the acidified coal slurry. This slurry was then added to a bioreactor. A pump was used to create fine bubbling on the surface for aeration. At time 0, 50 ml of slurry was removed for sulfate determination via known methods. The slurry was then inoculated with 20 cc purified Ferroxifunis bagdadii in feedstock and incubated at 37 °C. At various sampling times, 50 ml aliquots of slurry were removed and treated with 0.2 ml of 2% glutaraldehyde to stop microbial oxidation. These samples were stored at 5 °C until sulfate determinat ions were conducted. At day four, oxidation rates of 850 mg/1/hour were observed.
0.75 g/l K2HPO4, 0.75 g/l (NH4)2SO4) and 1500 ml distilled water were added to the jar. The contents of the jar were acidified to pH 2.2 with concentrated sulfuric acid. The mixture was shaken and then inoculated with 5cc purified
Ferroxifunis bagdadii in feedstock medium, containing 106 microorganisms. A control vessel, lacking the microorganism, was also established. The jars were incubated at 37 °C, without shaking. Samples were collected every six days for the detection of free copper via the addition of ammonium hydroxide. The presence of free copper was indicated by a color change from clear to blue. Free copper was detected after 36 months in chalcopyrite leach liquor from the inoculated ore. Passivation was observed in the non-inoculated ore after 19 months, with no free copper detected.
EXAMPLE 2 – TREATMENT OF TEXTILE WASTEWATER
Experimentation was performed to demonstrate that
Ferroxifunis bagdadii decolorizes the diazo dyes found in textile mill wastewaters. Purified Ferroxifunis bagdadii (2 ml feedstock) was added to 2 liters of distilled water containing
25 grams glutamic acid and 25 grams glucose. The pH of the solution was 3.8. After six days of microbial growth, dye waste effluent from the Oxford Textile firm in Oxford, New
Jersey was added to the solution. All color was removed within three days.
Claims (1)
What is claimed is
1. A substantially pure culture of Ferroxifunis bagdadii, having the identifying characteristics of ATCC 53601.
AU29016/89A
1987-12-10
1988-12-12
Microorganism for use in industrial processes
Granted
AU2901689A
(en)
Applications Claiming Priority (2)
Application Number
Priority Date
Filing Date
Title
US07/131,425
US4918018A
(en)
1987-12-10
1987-12-10
Microorganism for use in industrial processes
US131425
1987-12-10
Publications (1)
Publication Number
Publication Date
AU2901689A
true
AU2901689A
(en)
1989-07-05
Family
ID=22449411
Family Applications (1)
Application Number
Title
Priority Date
Filing Date
AU29016/89A
Granted
AU2901689A
(en)
1987-12-10
1988-12-12
Microorganism for use in industrial processes
Country Status (5)
Country
Link
US
(1)
US4918018A
(en)
AU
(1)
AU2901689A
(en)
CA
(1)
CA1301097C
(en)
WO
(1)
WO1989005341A1
(en)
ZW
(1)
ZW17588A1
(en)
Families Citing this family (5)
* Cited by examiner, † Cited by third party
Publication number
Priority date
Publication date
Assignee
Title
US5217615A
(en)
*
1991-02-25
1993-06-08
Institut National De La Recherche Scientifique
Bacterial leaching process and composition
WO1992019551A1
(en)
*
1991-04-30
1992-11-12
Institut National De La Recherche Scientifique
Semi-continuous bacterial leaching process
US5624844A
(en)
*
1995-06-02
1997-04-29
Energy Biosystems Corporation
Process for demetalizing a fossil fuel
ES2114809B1
(en)
*
1996-02-28
1999-02-01
Univ Salamanca
BACTERIAL STRAINS ABLE TO METABOLIZE TEXTILE DYES.
AUPQ468999A0
(en)
1999-12-15
2000-01-20
Pacific Ore Technology (Australia) Ltd
A bacterially assisted heap leach
Family Cites Families (6)
* Cited by examiner, † Cited by third party
Publication number
Priority date
Publication date
Assignee
Title
US3305353A
(en)
*
1964-03-30
1967-02-21
British Columbia Res Council
Accelerated microbiological ore extraction process
US3856913A
(en)
*
1972-09-21
1974-12-24
British Columbia Res Council
Copper extraction by rapid bacteriological process
US4483923A
(en)
*
1980-06-12
1984-11-20
Sybron Corporation
Microbiological process for removing non-ionic surface active agents, detergents and the like from wastewater and microorganism capable of same
US4376826A
(en)
*
1980-06-17
1983-03-15
Mynatt Roy L
Continuous production of bacteria for leaching of metallic ore
US4572898A
(en)
*
1982-12-14
1986-02-25
Genentech, Inc.
Thermophile isolate having thermostable hydrolytic activity
CA1214043A
(en)
*
1983-01-26
1986-11-18
Albert Bruynesteyn
Biological-acid leach process
1987
1987-12-10
US
US07/131,425
patent/US4918018A/en
not_active
Expired – Fee Related
1988
1988-12-12
CA
CA000585618A
patent/CA1301097C/en
not_active
Expired – Fee Related
1988-12-12
WO
PCT/US1988/004369
patent/WO1989005341A1/en
unknown
1988-12-12
AU
AU29016/89A
patent/AU2901689A/en
active
Granted
1988-12-12
ZW
ZW175/88A
patent/ZW17588A1/en
unknown
Also Published As
Publication number
Publication date
US4918018A
(en)
1990-04-17
CA1301097C
(en)
1992-05-19
ZW17588A1
(en)
1989-06-21
WO1989005341A1
(en)
1989-06-15
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