US2574070A - Purification of substances by microbial action - Google Patents
Purification of substances by microbial action Download PDFInfo
- Publication number
- US2574070A US2574070A US36441A US3644148A US2574070A US 2574070 A US2574070 A US 2574070A US 36441 A US36441 A US 36441A US 3644148 A US3644148 A US 3644148A US 2574070 A US2574070 A US 2574070A
- Authority
- US
- United States
- Prior art keywords
- action
- sulfate
- products
- vibrio
- microorganisms
- Prior art date
- 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.)
- Expired - Lifetime
Links
- 230000000813 microbial effect Effects 0.000 title claims description 6
- 239000000126 substance Substances 0.000 title description 4
- 238000000746 purification Methods 0.000 title description 3
- 229930195733 hydrocarbon Natural products 0.000 claims description 23
- 150000002430 hydrocarbons Chemical class 0.000 claims description 23
- 238000000034 method Methods 0.000 claims description 17
- 230000009471 action Effects 0.000 claims description 16
- 230000004060 metabolic process Effects 0.000 claims description 16
- 241000894006 Bacteria Species 0.000 claims description 13
- 241000607598 Vibrio Species 0.000 claims description 12
- 150000003464 sulfur compounds Chemical class 0.000 claims description 12
- 241000894007 species Species 0.000 claims description 9
- 241000589516 Pseudomonas Species 0.000 claims description 8
- 239000003208 petroleum Substances 0.000 claims description 7
- 241000588986 Alcaligenes Species 0.000 claims description 4
- 241000193830 Bacillus <bacterium> Species 0.000 claims description 4
- 241000605716 Desulfovibrio Species 0.000 claims description 4
- 244000005700 microbiome Species 0.000 description 22
- 239000000047 product Substances 0.000 description 19
- 239000004215 Carbon black (E152) Substances 0.000 description 10
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 10
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 9
- 229910052717 sulfur Inorganic materials 0.000 description 9
- 239000011593 sulfur Substances 0.000 description 9
- 230000008569 process Effects 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 7
- 239000003638 chemical reducing agent Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 239000012535 impurity Substances 0.000 description 5
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 5
- 239000010779 crude oil Substances 0.000 description 4
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000033116 oxidation-reduction process Effects 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000003209 petroleum derivative Substances 0.000 description 3
- 238000007670 refining Methods 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 235000015097 nutrients Nutrition 0.000 description 2
- 125000001741 organic sulfur group Chemical group 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 150000003463 sulfur Chemical class 0.000 description 2
- -1 tetraethyl lead Chemical class 0.000 description 2
- MRMOZBOQVYRSEM-UHFFFAOYSA-N tetraethyllead Chemical compound CC[Pb](CC)(CC)CC MRMOZBOQVYRSEM-UHFFFAOYSA-N 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 description 1
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- KRKNYBCHXYNGOX-UHFFFAOYSA-K Citrate Chemical compound [O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O KRKNYBCHXYNGOX-UHFFFAOYSA-K 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 229910021577 Iron(II) chloride Inorganic materials 0.000 description 1
- JVTAAEKCZFNVCJ-UHFFFAOYSA-M Lactate Chemical compound CC(O)C([O-])=O JVTAAEKCZFNVCJ-UHFFFAOYSA-M 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- MMDJDBSEMBIJBB-UHFFFAOYSA-N [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] Chemical compound [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] MMDJDBSEMBIJBB-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 229910052797 bismuth Inorganic materials 0.000 description 1
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000003009 desulfurizing effect Effects 0.000 description 1
- ZPWVASYFFYYZEW-UHFFFAOYSA-L dipotassium hydrogen phosphate Chemical compound [K+].[K+].OP([O-])([O-])=O ZPWVASYFFYYZEW-UHFFFAOYSA-L 0.000 description 1
- 229910000396 dipotassium phosphate Inorganic materials 0.000 description 1
- 235000019797 dipotassium phosphate Nutrition 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- IMBKASBLAKCLEM-UHFFFAOYSA-L ferrous ammonium sulfate (anhydrous) Chemical compound [NH4+].[NH4+].[Fe+2].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O IMBKASBLAKCLEM-UHFFFAOYSA-L 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000003630 growth substance Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000011534 incubation Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000011081 inoculation Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000000979 retarding effect Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 150000003722 vitamin derivatives Chemical class 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G32/00—Refining of hydrocarbon oils by electric or magnetic means, by irradiation, or by 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
- 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
- Y10S435/829—Alcaligenes
-
- 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
- Y10S435/832—Bacillus
-
- 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
- Y10S435/874—Pseudomonas
-
- 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
- Y10S435/909—Vibrio
Definitions
- This invention relates to the purification of substances including hydrocarbons and the like, and more particularly to the removal of sulfurbearing complexes or complex sulfur compounds from petroleum hydrocarbons.
- ,Crude oil in some cases, is characterized by the presence of objectionable quantities of sulfur compounds, mostly in complex form, which must be removed or substantially reduced in amount, dependent on the use of the final products, to eliminate possible corrosion by such final products when put in use.
- sulfur compounds are further objectionable in such final products as fuels for internal combustion engines in that they may tend to reduce the efliciency of antiknock compounds such as tetraethyl lead, and may, when used alone, reduce the octane number of the fuel.
- Such crudes cannot be handled by conventional refining methods because of the corrosive effect of the sulfur compounds. Modification of the usual refining processes plus additional steps are required in the refining of such crudes to either abstract the sulfur compounds or reduce them to unobjectionable amounts. require expensive and special apparatus, involve corrosion problems, and add materially to the cost of the final products.
- Pseudomonas bac-' teria and other microorganisms may metabolize the sulfur complexes in a petroleum hydrocarbon to sulfates which may then be used by them to attack hydrocarbons instead of the organic sulfur complexes. This will slow the metabolism to a point whereby the desired metabolism can be said to have reached equilibrium and will be halted. In the case of sulfur removal this is highly 0bjectionable.
- One object of this invention is to provide a novel process wherein the removal of so-called impurities from substances by microbial action is promoted.
- Another object of this invention is to provide a novel process wherein the metabolism of such impurities as complex sulfur compounds in petroleum hydrocarbons is maintained at a relatively rapid rate, the retarding or diverting effect of a Such process modifications product of the metabolism being substantially eliminated.
- Another object of this invention is the provision of a novel process wherein the removal of impurities such as complex sulfur compounds from petroleum hydrocarbons is rendered more complete.
- the present invention can be said to involve the removal as by conversion or metabolism of a relatively complex so-called impurity from a substance such as crude oil or hydrocarbon fractions by the action of selected microorganisms which act upon the impurity to form certain products of metabolism; and the action of different selected microorganisms which act upon the products of metabolism of the first microorganisms and convert such products to readily removable or separable products.
- the invention involves the metabolism or conversion in petroleum hydrocarbons of complex sulfur compounds to sulfates by the action of certain specific microorganisms, and the reduction of the sulfates to easily removed products such as hydrogen sulfideby sulfate-reducing microorganisms.
- bacteria such as certain species of Pseudomonas, Alcaligenes, Bacillus or other genera or any microorganisms which are capable of converting the sulfur-bearing complexes in a petroleum hydrocarbon to sulfates are grown in a mineral-salt nutrient medium in the presence of a small proportion, about 5 to 20%, of the petroleum hydrocarbon to be treated, and in the substantial absence of inorganic sulfur.
- mineral-salt nutrient medium in the presence of a small proportion, about 5 to 20%, of the petroleum hydrocarbon to be treated, and in the substantial absence of inorganic sulfur.
- min-, eral salt mediums or nutrient solutions are wellknown to the art, one example being formed of 1000 ml. of distilled water having the following mineral content:
- the medium may be further altered by the addition of pure accessory growth substances, i. e., vitamin and/or amino acids to promote growth of any desirable microorganism.
- the pH is preferably adjusted so that after sterilization, it is about 7.
- the addition of certain ions such as copper, mercury, zinc, bismuth and iodine to the medium in trace amounts may stimulate the activity of the microorganisms. Care must be exercised in the amount added since when such ions are present in more than trace amounts, they tend to poison the microorganism.
- Sulfate-reducing microorganisms such as bacteria of the anaerobic type (Vibrio desulfuricans, Vibrio estuarii, Vibrio thermodesulfuricans, or Desulfovibrio being mentioned by way of example) are grown in another lot of a, medium such as the following:
- the crude oil or hydrocarbon fraction to be processed is then inoculated with the two cultures, the sulfate reducer preferably being added after sulfate has become available from the organism attacking the sulfur complex.
- the conditions maintained are such as to encourage both metabolisms, i. e., the action of both sets of microorganisms.
- the conditions are such that the temperature is maintained within a range of 25 to 30 C. and the pH within a range of 6.5 to 7.5. In their action upon the hydrocarbon, the Pseudomonas.
- the sulfate producer functions to assimilate the sulfur-bearing complexes, the resultant end-product being sulfate with a small proportion of some water-soluble organic intermediate compounds.
- the sulfate would immediately operate to slow down or divert the action of the Pseudomonas and in time might halt its organic sulfur conversion completely
- the sulfate-reducing microorganism operates immediately to reduce substantially all the sulfate to hydrogen sulfide which may be readily removed.
- the Pseudomonas immediately produces more sulfate from the sulfur complex in the hydrocarbon, thereby effecting the destruction of more of the sulfur complex.
- the net effect is the continued removal of one of the products of the initial decomposition whereby the reaction proceeds to completion.
- the growth of the latter will reduce the oxidation-reduction potential in addition to producing sulfate so that the sulfate-reducer will encounter an environment more suited to its growth.
- Ammonium nitrate can be made available to satisfy the ammonium-nitrogen necessary for the growth of the sulfate-reducer, the nitrate-nitrogen also being available for the sulfate-producer which may also secure its oxygen therefrom. If the sulfate-producer is of a specie that cannot use oxygen in this form, citrate, lactate and equivalen'ts can be used where atmospheric oxygen is not available.
- the hydrogen sulfide produced by the sulfate-reducer may be removed as soon as formed by passing a relatively inert gas through the liquid.
- the gas can be cleaned subsequently of the hydrogen sulfide and recycled.
- hydrocarbon lost in this manner can be considered negligible.
- the principle of the invention may be applicable to processes other than the desulfurizing of hydrocarbons which has been discussed only by way of example.
- the process of the invention is applicable to any like processing wherein the products of the first metabolism are susceptible of conversion by a second microorganism or group of microorganisms to readily removable products.
- the desired specific action can proceed for a longer period of time, resulting in more complete action, and that the action of the first microorganisms, the sulfate-producer, is such as to produce and maintain the most favorable conditions for the second microorganisms, the sulfate-reducers.
- microorganisms as used herein is intended to include bacteria, their enzymes and other products as well as related fungi and molds.
- a method for converting or metabolizing relatively complex sulfur compounds in petroleum hydrocarbons to readily removable products by microbial action comprising the steps of subjecting hydrocarbons under metabolizing conditions to the action of bacteria selected from the class consisting of species of Pseudomonas, Alcaligenes and Bacillus, and subjecting the products of the metabolism to the action of sulfate-reducin bacteria selected from the class consisting of species of Vibrio desu lfuriwns, Vibrio estaurii, Vibrio thermodesulfuricans and Desulfovibrio.
- a method for converting or metabolizing relatively complex sulfur compounds in petroleum hydrocarbons to readily removable products by microbial action comprising the steps of subjecting hydrocarbons under metabolizing con- 5 ditions including a temperature in the range of 25 to 30 C. and a. pH in the range of 6.5 to 7.5 to the action of bacteria selected from the class consisting of species of Pseudomonas, Alcaligenes and Bacillus, and subjecting the products of the metabolism to the action of sulfate-reducin bacteria selected from the class consisting of species of Vibrio desulfuricans, Vibrio estuarii, Vibrio thermodesulfuricans and Desulfovibrio.
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Description
Patented Nov. 6, 1951 PURIFICATION OF SUBSTANQES BY MICROBIAL ACTIOH Raymond J. Strawinski, Long Beach, Calif., as-
signor to Texaco Development a Corporation, New York, N. Y., a corporation of Delaware No Drawing. Application July 1, 1948, Serial No. 36,441
4 Claims.
This invention relates to the purification of substances including hydrocarbons and the like, and more particularly to the removal of sulfurbearing complexes or complex sulfur compounds from petroleum hydrocarbons.
,Crude oil, in some cases, is characterized by the presence of objectionable quantities of sulfur compounds, mostly in complex form, which must be removed or substantially reduced in amount, dependent on the use of the final products, to eliminate possible corrosion by such final products when put in use. Such sulfur compounds are further objectionable in such final products as fuels for internal combustion engines in that they may tend to reduce the efliciency of antiknock compounds such as tetraethyl lead, and may, when used alone, reduce the octane number of the fuel. Such crudes cannot be handled by conventional refining methods because of the corrosive effect of the sulfur compounds. Modification of the usual refining processes plus additional steps are required in the refining of such crudes to either abstract the sulfur compounds or reduce them to unobjectionable amounts. require expensive and special apparatus, involve corrosion problems, and add materially to the cost of the final products.
While it is known that certain microorganisms will attack complex sulfur compounds, the action 01' such microorganisms is generally very slow and becomes slower as the extent of metabolism proceeds because of the accumulation of the products of metabolism which may be used in further metabolism by the microorganisms and therefore divert them from the originally desired activity.
To illustrate certain species of Pseudomonas bac-' teria and other microorganisms may metabolize the sulfur complexes in a petroleum hydrocarbon to sulfates which may then be used by them to attack hydrocarbons instead of the organic sulfur complexes. This will slow the metabolism to a point whereby the desired metabolism can be said to have reached equilibrium and will be halted. In the case of sulfur removal this is highly 0bjectionable.
One object of this invention is to provide a novel process wherein the removal of so-called impurities from substances by microbial action is promoted.
Another object of this invention is to provide a novel process wherein the metabolism of such impurities as complex sulfur compounds in petroleum hydrocarbons is maintained at a relatively rapid rate, the retarding or diverting effect of a Such process modifications product of the metabolism being substantially eliminated.
Another object of this invention is the provision of a novel process wherein the removal of impurities such as complex sulfur compounds from petroleum hydrocarbons is rendered more complete.
Other objects and advantages of the invention will appear from the following description and claims.
Briefly described, the present invention can be said to involve the removal as by conversion or metabolism of a relatively complex so-called impurity from a substance such as crude oil or hydrocarbon fractions by the action of selected microorganisms which act upon the impurity to form certain products of metabolism; and the action of different selected microorganisms which act upon the products of metabolism of the first microorganisms and convert such products to readily removable or separable products. More specifically, the invention involves the metabolism or conversion in petroleum hydrocarbons of complex sulfur compounds to sulfates by the action of certain specific microorganisms, and the reduction of the sulfates to easily removed products such as hydrogen sulfideby sulfate-reducing microorganisms.
As an illustration of an application of the invention, bacteria such as certain species of Pseudomonas, Alcaligenes, Bacillus or other genera or any microorganisms which are capable of converting the sulfur-bearing complexes in a petroleum hydrocarbon to sulfates are grown in a mineral-salt nutrient medium in the presence of a small proportion, about 5 to 20%, of the petroleum hydrocarbon to be treated, and in the substantial absence of inorganic sulfur. Such min-, eral salt mediums or nutrient solutions are wellknown to the art, one example being formed of 1000 ml. of distilled water having the following mineral content:
Grams NaH2PO4H2O 1 Kai-IP04 2 NH4NO3 2 MgClzfiHzO 0.25 MllCl24H2O 0.0 1 CaCOa 0.0 1 FeCl2 0.01
The medium may be further altered by the addition of pure accessory growth substances, i. e., vitamin and/or amino acids to promote growth of any desirable microorganism. The pH is preferably adjusted so that after sterilization, it is about 7. The addition of certain ions such as copper, mercury, zinc, bismuth and iodine to the medium in trace amounts may stimulate the activity of the microorganisms. Care must be exercised in the amount added since whensuch ions are present in more than trace amounts, they tend to poison the microorganism.
Sulfate-reducing microorganisms such as bacteria of the anaerobic type (Vibrio desulfuricans, Vibrio estuarii, Vibrio thermodesulfuricans, or Desulfovibrio being mentioned by way of example) are grown in another lot of a, medium such as the following:
K2HPO4 g 0.5 NHiCL g 1 MgSO4HI-I2O g 2 CaSO4.2HaO g 1 Nit-2804 g 1 ICaClzZI-IzO g 0.1 Crude oil g 3.5 Mohrs salt (ferrous ammonium sulfate) Trace H2O ml 1000 Incubation is under anaerobic conditions. After good growth is obtained, the culture is centrifuged and washed with 0.85% sterile saline solution to remove excess sulfate.
The crude oil or hydrocarbon fraction to be processed is then inoculated with the two cultures, the sulfate reducer preferably being added after sulfate has become available from the organism attacking the sulfur complex.
The conditions maintained are such as to encourage both metabolisms, i. e., the action of both sets of microorganisms. Preferably, the conditions are such that the temperature is maintained within a range of 25 to 30 C. and the pH within a range of 6.5 to 7.5. In their action upon the hydrocarbon, the Pseudomonas.
or other organism selected as the sulfate producer functions to assimilate the sulfur-bearing complexes, the resultant end-product being sulfate with a small proportion of some water-soluble organic intermediate compounds. Whereas the sulfate would immediately operate to slow down or divert the action of the Pseudomonas and in time might halt its organic sulfur conversion completely, the sulfate-reducing microorganism operates immediately to reduce substantially all the sulfate to hydrogen sulfide which may be readily removed. Thus the Pseudomonas immediately produces more sulfate from the sulfur complex in the hydrocarbon, thereby effecting the destruction of more of the sulfur complex. The net effect is the continued removal of one of the products of the initial decomposition whereby the reaction proceeds to completion.
By delaying the inoculation with the sulfatereducer until the first organism, i. e. the sulfateproducer has grown to some extent, the growth of the latter will reduce the oxidation-reduction potential in addition to producing sulfate so that the sulfate-reducer will encounter an environment more suited to its growth. Ammonium nitrate can be made available to satisfy the ammonium-nitrogen necessary for the growth of the sulfate-reducer, the nitrate-nitrogen also being available for the sulfate-producer which may also secure its oxygen therefrom. If the sulfate-producer is of a specie that cannot use oxygen in this form, citrate, lactate and equivalen'ts can be used where atmospheric oxygen is not available.
If the specific sulfate producing organism will not lower or maintain the necessary oxidationreduction potential for the anerobe, then a method of electrolytically controlling the potential can be used. A typical method is disclosed in a report in Archives of Biochemistry 2 183 (1943) by Martin E. Hanke and Gale J. Katz entitled "An Electrolytic Method for Controlling Oxidation-Reduction Potential and Its Application In The Study of Anaerobiosis." Under these conditions the reaction can be carried out in a stream of air.
If desired, the hydrogen sulfide produced by the sulfate-reducer may be removed as soon as formed by passing a relatively inert gas through the liquid. The gas can be cleaned subsequently of the hydrogen sulfide and recycled.
While some hydrocarbon may be converted by the microorganisms in the conversion of the sulfur complexes and the sulfates, the amount of hydrocarbon lost in this manner can be considered negligible.
The principle of the invention may be applicable to processes other than the desulfurizing of hydrocarbons which has been discussed only by way of example. The process of the invention is applicable to any like processing wherein the products of the first metabolism are susceptible of conversion by a second microorganism or group of microorganisms to readily removable products.
It will be noted that throughout the process described, the desired specific action can proceed for a longer period of time, resulting in more complete action, and that the action of the first microorganisms, the sulfate-producer, is such as to produce and maintain the most favorable conditions for the second microorganisms, the sulfate-reducers.
The term microorganisms as used herein is intended to include bacteria, their enzymes and other products as well as related fungi and molds.
Obviously many modifications and variations of the invention as above setforth may be made without departing from the spirit and scope thereof, and therefore only such limitations should be imposed as are indicated in the appended claims.
I claim:
1. A method for converting or metabolizing relatively complex sulfur compounds in petroleum hydrocarbons to readily removable products by microbial action comprising the steps of subjecting hydrocarbons under metabolizing conditions to the action of bacteria selected from the class consisting of species of Pseudomonas, Alcaligenes and Bacillus, and subjecting the products of the metabolism to the action of sulfate-reducin bacteria selected from the class consisting of species of Vibrio desu lfuriwns, Vibrio estaurii, Vibrio thermodesulfuricans and Desulfovibrio.
2. The method of claim 1 wherein said first mentioned bacteria are grown in a mineral-salt medium containing a small proportion of the hydrocarbon to be'treated and in the substantial absence of inorganic sulfur prior to charging the bacteria to the main portion of hydrocarbon to be treated.
3. The method of claim 1 wherein said firstmentioned bacteria are grown in a mineral-salt medium containing about 5 to 20% of the hydrocarbon to be treated and in the substantial absence of inorganic sulfur prior to chargin the bacteria to the main portion of the hydrocarbon to be treated.
4. A method for converting or metabolizing relatively complex sulfur compounds in petroleum hydrocarbons to readily removable products by microbial action comprising the steps of subjecting hydrocarbons under metabolizing con- 5 ditions including a temperature in the range of 25 to 30 C. and a. pH in the range of 6.5 to 7.5 to the action of bacteria selected from the class consisting of species of Pseudomonas, Alcaligenes and Bacillus, and subjecting the products of the metabolism to the action of sulfate-reducin bacteria selected from the class consisting of species of Vibrio desulfuricans, Vibrio estuarii, Vibrio thermodesulfuricans and Desulfovibrio.
RAYMOND J. STRAWINSKI.
REFERENCES crrEn UNITED STATES PATENTS Number Name Date 1,685,004 Mislin Sept. 18, 1928 1,753,641 Beckman Apr. 8, 1930 2,056,668 Bavin Oct. 6, 1936 2,291,009 Underkofller July 28, 1942 2,356,218 Christensen Aug. 22, 1944 2,413,278 Zobell Dec. 24, 1946 OTHER REFERENCES mausmn Microbiology, by Smyth & Obold, 1930 ed., page 244.
Claims (1)
1. A METHOD FOR CONVERTING OR METABOILIZING RELATIVELY COMPLEX SULFUR COMPOUNDS IN PETROLEUM HYDROCARBONS TO READILY REMOVABLE PRODUCTS BY MICROBIAL ACTION COMPRISING THE STEPS OF SUBJECTING HYDROCARBONS UNDER METABOILIZING CONDITIONS TO THE ACTION OF BACTERIA SELECTED FROM THE CLASS CONSISTING OF SPECIES OF PSEUDOMONAS, ALCALIGENES AND BACILLUS, AND SUBJECTING THE PRODUCTS OF THE METABOLISM TO THE ACTION OF SULFATE-REDUCING BACTERIA SELECTED FROM THE CLASS CONSISTING OF SPECIES OF VIBRIO DESULFURICANS, VIBRIO ESTAURII, VIBRIO THERMODESULFURICANS AND DESULFOVIBRIO.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US36441A US2574070A (en) | 1948-07-01 | 1948-07-01 | Purification of substances by microbial action |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US36441A US2574070A (en) | 1948-07-01 | 1948-07-01 | Purification of substances by microbial action |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2574070A true US2574070A (en) | 1951-11-06 |
Family
ID=21888623
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US36441A Expired - Lifetime US2574070A (en) | 1948-07-01 | 1948-07-01 | Purification of substances by microbial action |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2574070A (en) |
Cited By (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2880142A (en) * | 1956-12-10 | 1959-03-31 | Phillips Petroleum Co | Prospecting for petroleum deposits |
| US2975103A (en) * | 1956-04-06 | 1961-03-14 | Exxon Research Engineering Co | Bacteriological desulfurization of petroleum |
| US3020205A (en) * | 1958-10-09 | 1962-02-06 | Callahan Mining Corp | Recovery of sulfur from sulfates |
| US3310477A (en) * | 1964-11-27 | 1967-03-21 | Charles R Wilke | Method of isolating a desulfovibrio for use in removing sulfates from brine |
| US4108722A (en) * | 1976-12-10 | 1978-08-22 | Atlantic Richfield Company | Method for the restoration of an underground reservoir |
| US4124501A (en) * | 1977-08-04 | 1978-11-07 | University Of Southern California | Purifying oil shale retort water |
| US4242448A (en) * | 1979-04-12 | 1980-12-30 | Brown Robert S Iii | Regeneration of scrubber effluent containing sulfate radicals |
| WO1986001820A1 (en) * | 1984-09-18 | 1986-03-27 | Lambda Group, Inc. | Microbiological method for the removal of contaminants from coal |
| US4596778A (en) * | 1983-07-06 | 1986-06-24 | Phillips Petroleum Company | Single cell protein from sulfur energy sources |
| EP0126443A3 (en) * | 1983-05-18 | 1987-08-05 | The Standard Oil Company | A process for the selective preparation of microorganisms capable of reproducible reduction of sulfur and use of the microorganism for microbial desulfurization of coal |
| US4872986A (en) * | 1988-05-06 | 1989-10-10 | Sybron Chemicals, Inc. | Use of bacteria for control of algal bloom in wastewater, lagoons, or ponds |
| US5232854A (en) * | 1991-03-15 | 1993-08-03 | Energy Biosystems Corporation | Multistage system for deep desulfurization of fossil fuels |
| JPH06184557A (en) * | 1992-11-13 | 1994-07-05 | Agency Of Ind Science & Technol | Biological desulfurization method |
| US5472875A (en) * | 1991-05-01 | 1995-12-05 | Energy Biosystems Corporation | Continuous process for biocatalytic desulfurization of sulfur-bearing heterocyclic molecules |
| US5510265A (en) * | 1991-03-15 | 1996-04-23 | Energy Biosystems Corporation | Multistage process for deep desulfurization of a fossil fuel |
| US5593889A (en) * | 1990-11-21 | 1997-01-14 | Valentine; James M. | Biodesulfurization of bitumen fuels |
| US5874294A (en) * | 1990-11-21 | 1999-02-23 | Valentine; James M. | Biodesulfurization of fuels |
| US20030170874A1 (en) * | 2002-03-11 | 2003-09-11 | Isora Ranson | Biodesulfurization of hydrocarbons |
| EP1112386A4 (en) * | 1998-08-10 | 2005-02-16 | Clean Diesel Tech Inc | Improved microbial catalyst for desulfurization of fossil fuels |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1685004A (en) * | 1925-04-07 | 1928-09-18 | Joseph Franz Daubek | Method for increasing the usefulness of fodder and food |
| US1753641A (en) * | 1925-12-21 | 1930-04-08 | John W Beckman | Method of breaking emulsions |
| US2056668A (en) * | 1936-05-09 | 1936-10-06 | Specialty Sales Corp Ltd | Method of dehydrating oil emulsions |
| US2291009A (en) * | 1938-07-27 | 1942-07-28 | Chemical Foundation Inc | Production of diastatic material |
| US2356218A (en) * | 1941-09-02 | 1944-08-22 | Frank L Robinson | Fermentation process for production of ethanol |
| US2413278A (en) * | 1944-03-17 | 1946-12-24 | American Petroleum Inst | Bacteriological process for treatment of fluid-bearing earth formations |
-
1948
- 1948-07-01 US US36441A patent/US2574070A/en not_active Expired - Lifetime
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1685004A (en) * | 1925-04-07 | 1928-09-18 | Joseph Franz Daubek | Method for increasing the usefulness of fodder and food |
| US1753641A (en) * | 1925-12-21 | 1930-04-08 | John W Beckman | Method of breaking emulsions |
| US2056668A (en) * | 1936-05-09 | 1936-10-06 | Specialty Sales Corp Ltd | Method of dehydrating oil emulsions |
| US2291009A (en) * | 1938-07-27 | 1942-07-28 | Chemical Foundation Inc | Production of diastatic material |
| US2356218A (en) * | 1941-09-02 | 1944-08-22 | Frank L Robinson | Fermentation process for production of ethanol |
| US2413278A (en) * | 1944-03-17 | 1946-12-24 | American Petroleum Inst | Bacteriological process for treatment of fluid-bearing earth formations |
Cited By (22)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2975103A (en) * | 1956-04-06 | 1961-03-14 | Exxon Research Engineering Co | Bacteriological desulfurization of petroleum |
| US2880142A (en) * | 1956-12-10 | 1959-03-31 | Phillips Petroleum Co | Prospecting for petroleum deposits |
| US3020205A (en) * | 1958-10-09 | 1962-02-06 | Callahan Mining Corp | Recovery of sulfur from sulfates |
| US3310477A (en) * | 1964-11-27 | 1967-03-21 | Charles R Wilke | Method of isolating a desulfovibrio for use in removing sulfates from brine |
| US4108722A (en) * | 1976-12-10 | 1978-08-22 | Atlantic Richfield Company | Method for the restoration of an underground reservoir |
| US4124501A (en) * | 1977-08-04 | 1978-11-07 | University Of Southern California | Purifying oil shale retort water |
| US4242448A (en) * | 1979-04-12 | 1980-12-30 | Brown Robert S Iii | Regeneration of scrubber effluent containing sulfate radicals |
| EP0126443A3 (en) * | 1983-05-18 | 1987-08-05 | The Standard Oil Company | A process for the selective preparation of microorganisms capable of reproducible reduction of sulfur and use of the microorganism for microbial desulfurization of coal |
| US4596778A (en) * | 1983-07-06 | 1986-06-24 | Phillips Petroleum Company | Single cell protein from sulfur energy sources |
| WO1986001820A1 (en) * | 1984-09-18 | 1986-03-27 | Lambda Group, Inc. | Microbiological method for the removal of contaminants from coal |
| US4872986A (en) * | 1988-05-06 | 1989-10-10 | Sybron Chemicals, Inc. | Use of bacteria for control of algal bloom in wastewater, lagoons, or ponds |
| US5593889A (en) * | 1990-11-21 | 1997-01-14 | Valentine; James M. | Biodesulfurization of bitumen fuels |
| US5874294A (en) * | 1990-11-21 | 1999-02-23 | Valentine; James M. | Biodesulfurization of fuels |
| US5232854A (en) * | 1991-03-15 | 1993-08-03 | Energy Biosystems Corporation | Multistage system for deep desulfurization of fossil fuels |
| US5387523A (en) * | 1991-03-15 | 1995-02-07 | Energy Biosystems Corporation | Multistage process for deep desulfurization of fossil fuels |
| US5510265A (en) * | 1991-03-15 | 1996-04-23 | Energy Biosystems Corporation | Multistage process for deep desulfurization of a fossil fuel |
| US5472875A (en) * | 1991-05-01 | 1995-12-05 | Energy Biosystems Corporation | Continuous process for biocatalytic desulfurization of sulfur-bearing heterocyclic molecules |
| JPH06184557A (en) * | 1992-11-13 | 1994-07-05 | Agency Of Ind Science & Technol | Biological desulfurization method |
| JPH07103379B2 (en) | 1992-11-13 | 1995-11-08 | 工業技術院長 | Biodesulfurization |
| EP1112386A4 (en) * | 1998-08-10 | 2005-02-16 | Clean Diesel Tech Inc | Improved microbial catalyst for desulfurization of fossil fuels |
| US20030170874A1 (en) * | 2002-03-11 | 2003-09-11 | Isora Ranson | Biodesulfurization of hydrocarbons |
| US7338795B2 (en) * | 2002-03-11 | 2008-03-04 | Intevep, S.A. | Biodesulfurization of hydrocarbons |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2574070A (en) | Purification of substances by microbial action | |
| US2975103A (en) | Bacteriological desulfurization of petroleum | |
| JPS6012972A (en) | Biological desulfurization of coal | |
| US2521761A (en) | Method of desulfurizing crude oil | |
| US4954229A (en) | Bioelectrochemical desulfurization of petroleum | |
| CN110451638A (en) | A method of based on colony induction signaling molecule strengthened anaerobic ammoxidation sludge heavy-metal resistance | |
| Silva et al. | Optimization of low sulfur carob pulp liquor as carbon source for fossil fuels biodesulfurization | |
| CN113862198A (en) | Compound microbial agent for degrading oil pollutants in oily sludge and preparation method and application thereof | |
| CA1172591A (en) | Catalytic water wash | |
| CN103923867B (en) | Mixed bacterial microbial preparation and in process containing the application in nitric nitrogen waste water | |
| Chang et al. | Production of a desulfurization biocatalyst by two‐stage fermentation and its application for the treatment of model and diesel oils | |
| US4456688A (en) | Microbiological desulfurization of coal | |
| US3069325A (en) | Treatment of hydrocarbons | |
| US4314902A (en) | Catalytic water wash | |
| IE47023B1 (en) | Biological denitrification of effluents | |
| EP0082814A1 (en) | Microorganisms of the genus pseudomonas and method for the decomposition of compounds containing methyl groups in aqueous solutions | |
| CN103880194A (en) | Microorganism water purification agent and preparation method thereof | |
| Acharya et al. | Biodepyritisation of coal | |
| CN107684821B (en) | Biofiltration filler for VOCs and malodorous gas treatment and preparation method thereof | |
| Takeda et al. | Production of microbial cells from hydrocarbons | |
| US3310477A (en) | Method of isolating a desulfovibrio for use in removing sulfates from brine | |
| CN112279383A (en) | Microbial water purifying agent for rapidly reducing ammonia nitrogen index in water body and preparation method thereof | |
| Shelobolina et al. | Microorganisms of kaolins and their role in the processes of iron solubilization and transformation | |
| RU2039815C1 (en) | Strain of bacteria desulfomicrobarium bacilatum which is used for purification of sewage against ions of heavy metals | |
| KR0147744B1 (en) | Cyanide decomposed strain and thiocyanide decomposed strain, and wastewater containing cyanide and thiocyanide using this decomposed strain |