CA2109477C - Injection of organic phosphates for subterranean microbial processes - Google Patents
Injection of organic phosphates for subterranean microbial processesInfo
- Publication number
- CA2109477C CA2109477C CA002109477A CA2109477A CA2109477C CA 2109477 C CA2109477 C CA 2109477C CA 002109477 A CA002109477 A CA 002109477A CA 2109477 A CA2109477 A CA 2109477A CA 2109477 C CA2109477 C CA 2109477C
- Authority
- CA
- Canada
- Prior art keywords
- nutrient
- organic
- phosphorus
- microbial
- subterranean formation
- 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 - Fee Related
Links
- 229910019142 PO4 Inorganic materials 0.000 title claims abstract description 29
- 235000021317 phosphate Nutrition 0.000 title claims description 26
- 238000002347 injection Methods 0.000 title abstract description 15
- 239000007924 injection Substances 0.000 title abstract description 15
- 150000003013 phosphoric acid derivatives Chemical class 0.000 title description 6
- 230000007483 microbial process Effects 0.000 title description 4
- 235000015097 nutrients Nutrition 0.000 claims abstract description 44
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 41
- 238000005755 formation reaction Methods 0.000 claims abstract description 41
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 34
- 239000011574 phosphorus Substances 0.000 claims abstract description 34
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 31
- 238000000034 method Methods 0.000 claims abstract description 31
- 230000000813 microbial effect Effects 0.000 claims abstract description 28
- 239000010452 phosphate Substances 0.000 claims abstract description 22
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims abstract description 21
- 230000002950 deficient Effects 0.000 claims abstract description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 14
- 229910052799 carbon Inorganic materials 0.000 claims description 14
- 239000002253 acid Substances 0.000 claims description 7
- 125000000217 alkyl group Chemical group 0.000 claims description 7
- 238000011084 recovery Methods 0.000 claims description 6
- 229920000137 polyphosphoric acid Polymers 0.000 claims description 4
- 125000004432 carbon atom Chemical group C* 0.000 claims description 3
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 3
- 235000014786 phosphorus Nutrition 0.000 description 31
- 244000005700 microbiome Species 0.000 description 19
- 239000012267 brine Substances 0.000 description 17
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 17
- 150000001875 compounds Chemical class 0.000 description 15
- 239000011435 rock Substances 0.000 description 11
- 230000035699 permeability Effects 0.000 description 9
- 230000012010 growth Effects 0.000 description 7
- -1 potassium nitrate Chemical compound 0.000 description 7
- 239000000243 solution Substances 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 229910052816 inorganic phosphate Inorganic materials 0.000 description 6
- 238000001179 sorption measurement Methods 0.000 description 6
- 238000011065 in-situ storage Methods 0.000 description 5
- 150000003014 phosphoric acid esters Chemical class 0.000 description 5
- 238000001556 precipitation Methods 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 239000002028 Biomass Substances 0.000 description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 230000000717 retained effect Effects 0.000 description 4
- 229910052708 sodium Inorganic materials 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 3
- 230000001580 bacterial effect Effects 0.000 description 3
- 229920005549 butyl rubber Polymers 0.000 description 3
- 150000001720 carbohydrates Chemical class 0.000 description 3
- 235000014633 carbohydrates Nutrition 0.000 description 3
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 3
- 239000008103 glucose Substances 0.000 description 3
- 238000011534 incubation Methods 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- UGTZMIPZNRIWHX-UHFFFAOYSA-K sodium trimetaphosphate Chemical compound [Na+].[Na+].[Na+].[O-]P1(=O)OP([O-])(=O)OP([O-])(=O)O1 UGTZMIPZNRIWHX-UHFFFAOYSA-K 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- 229920000388 Polyphosphate Polymers 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- CAAULPUQFIIOTL-UHFFFAOYSA-N methyl dihydrogen phosphate Chemical compound COP(O)(O)=O CAAULPUQFIIOTL-UHFFFAOYSA-N 0.000 description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 230000035515 penetration Effects 0.000 description 2
- 239000001205 polyphosphate Substances 0.000 description 2
- 235000011176 polyphosphates Nutrition 0.000 description 2
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 2
- LWIHDJKSTIGBAC-UHFFFAOYSA-K potassium phosphate Substances [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 210000002966 serum Anatomy 0.000 description 2
- LIMXEVCFAUTBCK-UHFFFAOYSA-N 2,5-dibromo-3-methylpyridine Chemical compound CC1=CC(Br)=CN=C1Br LIMXEVCFAUTBCK-UHFFFAOYSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical group OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- DPKHZNPWBDQZCN-UHFFFAOYSA-N acridine orange free base Chemical compound C1=CC(N(C)C)=CC2=NC3=CC(N(C)C)=CC=C3C=C21 DPKHZNPWBDQZCN-UHFFFAOYSA-N 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- AWUCVROLDVIAJX-UHFFFAOYSA-N alpha-glycerophosphate Natural products OCC(O)COP(O)(O)=O AWUCVROLDVIAJX-UHFFFAOYSA-N 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 239000012491 analyte Substances 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- DZBUGLKDJFMEHC-UHFFFAOYSA-N benzoquinolinylidene Natural products C1=CC=CC2=CC3=CC=CC=C3N=C21 DZBUGLKDJFMEHC-UHFFFAOYSA-N 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- FJTUUPVRIANHEX-UHFFFAOYSA-N butan-1-ol;phosphoric acid Chemical compound CCCCO.OP(O)(O)=O FJTUUPVRIANHEX-UHFFFAOYSA-N 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 159000000007 calcium salts Chemical class 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 230000010261 cell growth Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 235000011180 diphosphates Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000011067 equilibration Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 229920000912 exopolymer Polymers 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000009616 inductively coupled plasma Methods 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 125000001477 organic nitrogen group Chemical group 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- IBIRZFNPWYRWOG-UHFFFAOYSA-N phosphane;phosphoric acid Chemical compound P.OP(O)(O)=O IBIRZFNPWYRWOG-UHFFFAOYSA-N 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000004323 potassium nitrate Substances 0.000 description 1
- 235000010333 potassium nitrate Nutrition 0.000 description 1
- 235000011009 potassium phosphates Nutrition 0.000 description 1
- 102000004196 processed proteins & peptides Human genes 0.000 description 1
- 108090000765 processed proteins & peptides Proteins 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- AWUCVROLDVIAJX-GSVOUGTGSA-N sn-glycerol 3-phosphate Chemical compound OC[C@@H](O)COP(O)(O)=O AWUCVROLDVIAJX-GSVOUGTGSA-N 0.000 description 1
- 239000001488 sodium phosphate Substances 0.000 description 1
- 235000011008 sodium phosphates Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 230000002459 sustained effect Effects 0.000 description 1
- DQWPFSLDHJDLRL-UHFFFAOYSA-N triethyl phosphate Chemical compound CCOP(=O)(OCC)OCC DQWPFSLDHJDLRL-UHFFFAOYSA-N 0.000 description 1
- 229920003169 water-soluble polymer Polymers 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/84—Compositions based on water or polar solvents
- C09K8/86—Compositions based on water or polar solvents containing organic compounds
- C09K8/88—Compositions based on water or polar solvents containing organic compounds macromolecular compounds
- C09K8/90—Compositions based on water or polar solvents containing organic compounds macromolecular compounds of natural origin, e.g. polysaccharides, cellulose
- C09K8/905—Biopolymers
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/58—Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Fertilizers (AREA)
- Agricultural Chemicals And Associated Chemicals (AREA)
Abstract
The present invention provides a process for sustaining microbial activity in subterranean formations which comprises introducing as a microbial nutrient, an organic phosphate. This process may include the sequential injection of sources of individual nutrient components which are deficient in said subterranean formation, whereby the injected phosphorus source is an organic phosphate.
Description
3307lCA
2109~77 THE INJECTION O~ ORGANIC PHOSPHATES FOR
SUBTERRANEAN MICROBIAL PROGESSES
This invention relates to the use of organic phosphates as nutrients in a method for sustaining microbial activity in subterranean formations.
BACKGROUND
In many subterranean microbial processes, nutrient selection and injection are controlling factors to successful operations. The microorganisms utilized must be nutritiously sustained and metabolically active and thus able to achieve their specific objective.
Numerous microorganisms suitable for achieving various microbial objectives in subterranean formations are known in the art. In order to achieve a specific microbial objective, suitable mlcroorganisms can be selected and injected into the subterranean fcrmation. Oftentimes, however, endogenous microorganisms well suited for achieving a particular microbial objective are already present within the formation.
Recently, a method was disclosed by Clark, et al. (Patent No.
5,083,611 assigned to Phillips Petroleum ~ompany), which overcame many problems associated with microbial nutrient injection methods then known to the art. This newly disclosed method provides for the sequential injection into a subterranean formation of sources of individual nutrient components which are deficient in the subterranean formation so that a complete nutrient medium capable of sustairling substantial microbial acti~ity is formed in the *
3307lCA
2109~77 THE INJECTION O~ ORGANIC PHOSPHATES FOR
SUBTERRANEAN MICROBIAL PROGESSES
This invention relates to the use of organic phosphates as nutrients in a method for sustaining microbial activity in subterranean formations.
BACKGROUND
In many subterranean microbial processes, nutrient selection and injection are controlling factors to successful operations. The microorganisms utilized must be nutritiously sustained and metabolically active and thus able to achieve their specific objective.
Numerous microorganisms suitable for achieving various microbial objectives in subterranean formations are known in the art. In order to achieve a specific microbial objective, suitable mlcroorganisms can be selected and injected into the subterranean fcrmation. Oftentimes, however, endogenous microorganisms well suited for achieving a particular microbial objective are already present within the formation.
Recently, a method was disclosed by Clark, et al. (Patent No.
5,083,611 assigned to Phillips Petroleum ~ompany), which overcame many problems associated with microbial nutrient injection methods then known to the art. This newly disclosed method provides for the sequential injection into a subterranean formation of sources of individual nutrient components which are deficient in the subterranean formation so that a complete nutrient medium capable of sustairling substantial microbial acti~ity is formed in the *
3307lCA
2 2109~77 subterranean formation upon injection of the last nutrient source. Each of the nutrient sources is comprised of at least one of the deficient individual nutrient components. Further, each of the nutrient sources, up to and including the next to the last nutrient source injected, is injected in an amount such that at least one individual nutrient component contained therein is retained in the subterranean formation in an amount sufficient for achieving the desired in-situ microbial objective.
The above method prevents the excessive utilization and depletion of nutrient components by microorganisms located in the vicinity of the borehole and also takes advantage of chromatographic retention in order to achieve nutrient media distribution beyond the proximity of the borehole. However, it has been discovered and is disclosed by the present application, that in order to achieve biomass production (i.e. microbial growth and/or exopolymer production) to plug lligh permeability zones within subterranean formations, a specific phosphorus source when used in the method of Patent 5,083,611 exhibits greater plugging potential than others presently used. The phosphorus source of the present invention is an organic phosphate which is used in combination with a carbon source, and provides for an unexpected increase in a capacity for the desired plugging, due to the ability of said phosphonls source to be more easily transported. The ability of the nutrients to be transported in-depth is therefore of great importance. Some problems associated with the use of known phosphorus sources such as inorganic phosphates is their tendency to complex with divalent cations within the reservoir which results in poor solubility and heightened difficulty transport distal to the wellbore. Also, inorganic polyphosphates hydrolyze at higher temperatures which render them less soluble in hard brines characterized by such temperatures. Thus, the specific use of organic phosphates as the phosphorus source in the above method, significantly contributes to the art of practicing said method.
It is therefore an object of this invention to provide a phosphorus source for use in the state-of-the art nutrient injection for subterranean microbial processes which provides for greatly enhanced transportability and thermal stability of the phosphorus nutrient.
These and other objects of the present invention will become apparent upon inspection of the disclosure and the claims herein provided.
SUMNARY OF THE INVENTION
In accordance with the present invention, we have discovered that when injected as the phosphorus source in subterranean microbial processes, organic phosphates are more readily transportable than those known in the art and are thermally stable, thus allowing biological activity to be achieved.
A process is therefore provided for sustaining microbial activity in subterranean formations which comprises introducing as a microbial nutrient, an organic phosphate.
DETAILED DESCRIPTION
The phosphorus nutrient injection system disclosed herein can generally be used in conjunction with any process wherein microbial activity is induced in a subterranean formation. Examples of such processes include microbial enhanced oil recovery, (MEOR) processes used in oil-bearing subterranean formations, and bioremediation processes used in aquifers.
Typical microbial enhanced oil recovery processes include those wherein microorganisms are used to alter subterranean formation permeability and those wherein microorganisms are used for in-situ generation of chemicals useful for enhanced oil recovery. Examples of in-situ generated chemicals include water-soluble polymers, surfactants, solvents such as ethanol and acetone, acids, carbon dioxide, etc.
The present inventive nutrient combination of an organic phosphate and a carbon source is particularly well suited for use in conjunction with MEOR processes for improving the volumetric sweep efficiency of subterranean formations. Oil-bearing subterranean formations contain porous rock with heterogenous zones of permeability. Water, used to mobilize oil in a waterflood, preferentially invades the high permeability zones due to these zones' decreased resistance to flow. This causes large reserves of oil, contained in the lower permeability regions, to be bypassed. In microbial enhanced oil recovery processes, nutrients are fed to microorganisms located in high permeability formation zones. The nutrients stimulate the microorganisms and cause the microorganisms to generate an increased biomass.
This increased biomass results from cell growth and/or the biological production of polymer(s). Once the high permeability formation zones have been plugged, water is diverted to the previously uninvaded low permeability zones and thereby displaces oil contained in the low permeability zones.
The microorganisms used in conjunction with the present invention are selected for the attainment of a desired microbial objective and then injected into the subterranean formation. Preferably, such microorganisms when used, are injected into the formation prior to nutrient injection. As is known in the art, the particular microorganisms chosen for injection should be tolerant of the conditions, e.g., temperature, pH, salinity etc., existing in the formation. Microorganisms can be injected into subterranean formations using methods which are well known in the art. The preferred microorganism injection method will depend upon the microorganism(s) chosen, and the specific characteristics of the formation. Oftentimes, endogenous microorganisms capable of achieving a desired microbial objective are already present within the subterranean formation. In order to cause the microorganisms within a subterranean formation, whether endogenous or injected, to produce a desired in-situ result, deficient nutrient components are injected into the formation which facilitates the regulation of where, in the formation, a complete nutrient package is formed and hence microbial activity occurs. Deficient nutrient components are those individual nutrient components which are needed by the microorganisms for achievement of a desired microbial objective and which are not already present within the formation in amounts sufficient for achieving the microbial objective. Subterranean formations are typically deficient in either phosphorus, nitrogen, or carbon nutrients, or combinations thereof. Suitable phosphorus sources and nitrogen sources (e.g., ammonium-containing compounds such as ammonium chloride, nitrates such as potassium nitrate, and organic nitrogen sources such as amino acids and peptides), as well as carbon sources (e.g., fats, proteins, simple carbohydrates and complex carbohydrates), and other nutrient sources which are suitable for use in nutrient injection methods are well known in the art.
However, selection of a phosphorus source which is sufficiently deficient in carbon and nitrogen and which causes increased in-situ biomass production at depths of penetration where plugging is most desirable is extremely beneficial in the practice of the above method. The inventive use of organic phosphates as the phosphorus source results in an unexpected increase in microbial activity at desired plugging sites due to the ability of the organic phosphate to be easily transported and to maintain a high thermal stability.
The term organic phosphate as used herein, refers to any compound or mixture of compounds containing the general molecular structure of phosphoric 3~07].~
or polyphosphoric acid namely, l(~lO)3PO] , in which at least one. hydrogen atom is replaced by an organic re~idue; and n is a number from 1 to about 10.
Thus, the or~anic phosphate of the present i.nvention can either origlnate as a monophosphoric acid or a polyphosphoric acid in which the phosphoric acid residues are covalently linked e.g.
O O O
Il li !l R - O - P - O - P - O - P - OH
I
~H OH G~
The or~anic residues inc~ude but are not limited to alkyl groups, and preferrea organic residues are those having the carbon content of 1 to about 17 carbon atoms per molecule. Organic residues are l.inked to the phosphoru~ atom via an ester hond. Examples of appropriate org~nic residue.s include but are Dot limited to m~thyl, ethyl, ~utyl, carbohydrates, proteins, p~ptides and lipids.
The carbon source to be used in combination with an organic phosphate phosphorus source should be in a substantially phospllorus-nutrierlt-free solutiorl, Also, the or~anic phosphflte should be in a substantia'lly carbon-nutrient-free solution, i.e., a solution sufficiently defici~,nt in carbon to render it unusable as a carbon source by the targeted microorganisms. This is to avoid achieving a complete nutrient combination and thus micr~.>b,.al actl~ity prior to locating the nutrients i.n a positi.on in the subterra.nean formation where m.icrob.'al acti~rity i~ most desired~
Therefore it is sdvarltageous to first iniect a phosphorus solution of organic phosphate which is more reAdi~y ret~.ned in the su~terranean formatior~ and 3307lCA
7 2109~77 thereafter inject a substantially phosphorus-nutrient-free carbon solution.
This permits deep penetration of the phosphorus prior to the injection of the carbon source which has less retainability in the subterranean formation. The carbon nutrient solution, being substantially phosphorus free will ultimately catch up to the previously injected phosphorus solution and form a complete nutrient combination deep within the subterranean formation. Microbial activity will occur where a complete nutrient combination exists and thus where such activity is most desired. Such method is well suited for enhancing oil recovery from oil-bearing subterranean formations.
The following example has been provided merely to illustrate the practice of the invention and should not be read as to limit the scope of the invention or the appended claims in any way.
EXAMPLES
Example I
Three screening criteria were used to determine the preferred use of organic phosphates vs. inorganic phosphate as sources of phosphorus for biological growth and metabolism. The criteria screened included the ability of the compound to support growth, the adsorption of the compound to rock, and the precipitation of the compound in the brine.
All tests were performed with field brine collected from a skimmer tank at the tract 5 tank battery located at the North Burbank Unit, Osage County, Oklahoma. Burbank brine is typical of many highly mineralized, oil-reservoir brines in that a large percentage of the solids are sodium and calcium salts (Table 1). The temperature of the brine under reservoir 3307lCA
8 21~9477 conditions is between 40 and 45C which is moderate for many oil reservoirs.
Brine samples were collected in glass bottles pre-incubated in an anaerobic glove box to remove oxygen. Bottles were capped with a butyl rubber septum.
The septum was penetrated with a 22 gauge hypodermic needle attached to a 1/4 inch (ID) nylon tubing that was used to transmit the brine sample into the bottle. Bottles of brine were transported back to the lab the same day and placed in the anaerobic glove box.
Table l Chemical Analysis of Injection Brine from the Tract 5 Tank Battery at the North Burbank Unit Analyte Concentration (g/L) ammonium .033 nitrate <.005 nitrate <.005 sulfate .020 phosphate <.050 total organic carbon .025 calcium 6.290 barium .755 magnesium 1.250 sodium 31.000 chloride 63.000 iron .0168 total dissolved solids127.300 Adsorption Screen Brine was filtered through a 0.22 micron membrane filter and enough organic phosphate ester (OP~) compound added to the brine to get a final phosphorus concentration of approximately 100 mg/L. This solution was added to a serum bottle containing 1 gram of crushed and sieved Burbank rock. The bottle was stoppered with a butyl rubber stopper and placed on a New Brunswick orbital shaker-incubator at 40C. In a like manner, sodium trimetaphosphate 3307lCA
9 2109~77 (STMP), an inorganic polyphosphate, was added to another bottle containing crushed rock and brine and incubated at 40C.
After 72 hours incubation the sample was filtered to remove the rock and the filtrate assayed for phosphorus. The phosphorus was detected using inductively coupled plasma analysis. The phosphorus detected in the filtrate is indicative of the amount of non-adsorbing or non-retained phosphorus compound after equilibration with the rock.
An index was established that compares the efficacy of the test OPE
to an inorganic phosphate, i.e., STMP. STMP was found to be more soluble in this brine as compared to other inorganic phosphates tested (e.g. sodium and potassium phosphates as well as pyrophosphates); however, its propensity to chemically degrade, at the temperature tested, to the highly insoluble ortho-phosphate made it an unattractive candidate. Therefore, STMP became a standard by which to gauge the effectiveness of other test compounds, that is, effective compounds would have to display properties superior STMP to in terms of adsorption or retention and chemical stability (i.e. precipitation).
The adsorption index (AI) was defined as the amount of STMP
phosphorus adsorbed by 1.0 gram of rock at 40C divided by the amount of OPE
adsorbed per gram of rock at 40C. An AI greater than 1.0 indicates the test compound relative to STMP is superior in terms of its inability to be retained by the rock. Subsequently, all compounds that were retained less than STMP
were considered preferred candidates for transport through the rock matrix.
As can be seen in Table 2, all OPEs tested had AIs greater than 1Ø
Precipitation Screen Samples were prepared as above for the adsorption screen except that no crushed rock was present in the bottles and the samples were held at 40C
for 23 days instead of 3 days. The long term precipitation index (LTPI) is 3307lCA
lO 2109477 defined as the weight of dissolved phosphorus in the brine after 23 days divided by the weight of dissolved phosphorus in deionized water after 3 days at room temperature. The LTPI is a measure of the chemical stability of the test compounds. Those compounds that are less likely to precipitate in brine at the higher temperature are those that have LPTIs close to 1Ø Table 2 shows that all the OPEs tested has LTPIs close to 1.0 and greater than that for STMP. For the purposes of this screen all compounds with LPTIs greater than STMP were considered to be superior and thus preferred compounds.
Table 2 Adsorption and Long Term Precipitation Indices for Various Organic Phosphate Esters Organic phosphate ester Source AI LTPI
Triethylphosphate Kodak 13.0 0.86 Methyl acid phosphate Albright-Wilson 31.0 1.05 Dimethyl acid pyrophosphate Albright-Wilson 1.08 0.88 Ethyl acid phosphate Akzo 5.40 0.97 Butyl acid phosphate Akzo 1.20 1.01 Monomethylphosphate Sigma 65.0 0.90 Sodium Trimetaphosphate Monsanto 1.0 0.64 Biological Screen These screens were performed by adding 100 mL of unfiltered Burbank brine to sterile, 120 mL serum bottles. Additions were made in an anaerobic glove box to prevent contamination by oxygen. Glucose was added at a final concentration of 0.1 percent and a phosphorus compound added at a final concentration of 100 micromolar, as phosphorus. The bottles were stoppered 3307lCA
with butyl rubber stoppers and incubated at 45C for two weeks. After incubation, the bo-ttles were sampled and bacterial numbers determined as acridine orange direct counts (AODC). In addition, the pH of the sample was measured. A lowering of pH along with an increase in cell count is indicative of bacterial fermentation of the glucose. The phosphorus compound was considered to support growth if it could stimulate an increase in bacterial numbers and lower pH to levels comparable to that obtained by using glucose plus STMP. The results in Table 3 show that four OPE supported growth and pH
declines similar to that of STMP. Therefore OPEs can better serve as effective phosphorus sources for biological growth when compared to the more commonly used inorganic phosphates.
Table 3 Comparison of the Ability of Organic Phosphate Esters vs.
Inorganic Phosphate to Support Growth of Bacteria in Burbank Brine after two Weeks Incubation at 45C
Phosphate ester Source pH AODC (X 108) bacteria/mL
Sodium Trimetaphosphate Monsanto 5.0 1.5 Alpha-glycerophosphate Sigma 5.0 2.9 Monomethyl phosphate Sigma 5.05 1.2 Ethyl acid phosphate Akzo 5.1 1.85 Methyl acid phosphate Albright-Wilson 5.05 0.62 Sodium Trimetaphosphateb Sigma 5.0 0.86 NOTE: Controls without a phosphorus source had average pH values of 6.1 and AODCs of .02 X 108 bacteria/mL.
, averages for two replicates; a, rbsults obtained with the same batch ofbrine collected on May 11, 1990; , results obtained with the same batch of brine collected on August 13, 1990.
The above method prevents the excessive utilization and depletion of nutrient components by microorganisms located in the vicinity of the borehole and also takes advantage of chromatographic retention in order to achieve nutrient media distribution beyond the proximity of the borehole. However, it has been discovered and is disclosed by the present application, that in order to achieve biomass production (i.e. microbial growth and/or exopolymer production) to plug lligh permeability zones within subterranean formations, a specific phosphorus source when used in the method of Patent 5,083,611 exhibits greater plugging potential than others presently used. The phosphorus source of the present invention is an organic phosphate which is used in combination with a carbon source, and provides for an unexpected increase in a capacity for the desired plugging, due to the ability of said phosphonls source to be more easily transported. The ability of the nutrients to be transported in-depth is therefore of great importance. Some problems associated with the use of known phosphorus sources such as inorganic phosphates is their tendency to complex with divalent cations within the reservoir which results in poor solubility and heightened difficulty transport distal to the wellbore. Also, inorganic polyphosphates hydrolyze at higher temperatures which render them less soluble in hard brines characterized by such temperatures. Thus, the specific use of organic phosphates as the phosphorus source in the above method, significantly contributes to the art of practicing said method.
It is therefore an object of this invention to provide a phosphorus source for use in the state-of-the art nutrient injection for subterranean microbial processes which provides for greatly enhanced transportability and thermal stability of the phosphorus nutrient.
These and other objects of the present invention will become apparent upon inspection of the disclosure and the claims herein provided.
SUMNARY OF THE INVENTION
In accordance with the present invention, we have discovered that when injected as the phosphorus source in subterranean microbial processes, organic phosphates are more readily transportable than those known in the art and are thermally stable, thus allowing biological activity to be achieved.
A process is therefore provided for sustaining microbial activity in subterranean formations which comprises introducing as a microbial nutrient, an organic phosphate.
DETAILED DESCRIPTION
The phosphorus nutrient injection system disclosed herein can generally be used in conjunction with any process wherein microbial activity is induced in a subterranean formation. Examples of such processes include microbial enhanced oil recovery, (MEOR) processes used in oil-bearing subterranean formations, and bioremediation processes used in aquifers.
Typical microbial enhanced oil recovery processes include those wherein microorganisms are used to alter subterranean formation permeability and those wherein microorganisms are used for in-situ generation of chemicals useful for enhanced oil recovery. Examples of in-situ generated chemicals include water-soluble polymers, surfactants, solvents such as ethanol and acetone, acids, carbon dioxide, etc.
The present inventive nutrient combination of an organic phosphate and a carbon source is particularly well suited for use in conjunction with MEOR processes for improving the volumetric sweep efficiency of subterranean formations. Oil-bearing subterranean formations contain porous rock with heterogenous zones of permeability. Water, used to mobilize oil in a waterflood, preferentially invades the high permeability zones due to these zones' decreased resistance to flow. This causes large reserves of oil, contained in the lower permeability regions, to be bypassed. In microbial enhanced oil recovery processes, nutrients are fed to microorganisms located in high permeability formation zones. The nutrients stimulate the microorganisms and cause the microorganisms to generate an increased biomass.
This increased biomass results from cell growth and/or the biological production of polymer(s). Once the high permeability formation zones have been plugged, water is diverted to the previously uninvaded low permeability zones and thereby displaces oil contained in the low permeability zones.
The microorganisms used in conjunction with the present invention are selected for the attainment of a desired microbial objective and then injected into the subterranean formation. Preferably, such microorganisms when used, are injected into the formation prior to nutrient injection. As is known in the art, the particular microorganisms chosen for injection should be tolerant of the conditions, e.g., temperature, pH, salinity etc., existing in the formation. Microorganisms can be injected into subterranean formations using methods which are well known in the art. The preferred microorganism injection method will depend upon the microorganism(s) chosen, and the specific characteristics of the formation. Oftentimes, endogenous microorganisms capable of achieving a desired microbial objective are already present within the subterranean formation. In order to cause the microorganisms within a subterranean formation, whether endogenous or injected, to produce a desired in-situ result, deficient nutrient components are injected into the formation which facilitates the regulation of where, in the formation, a complete nutrient package is formed and hence microbial activity occurs. Deficient nutrient components are those individual nutrient components which are needed by the microorganisms for achievement of a desired microbial objective and which are not already present within the formation in amounts sufficient for achieving the microbial objective. Subterranean formations are typically deficient in either phosphorus, nitrogen, or carbon nutrients, or combinations thereof. Suitable phosphorus sources and nitrogen sources (e.g., ammonium-containing compounds such as ammonium chloride, nitrates such as potassium nitrate, and organic nitrogen sources such as amino acids and peptides), as well as carbon sources (e.g., fats, proteins, simple carbohydrates and complex carbohydrates), and other nutrient sources which are suitable for use in nutrient injection methods are well known in the art.
However, selection of a phosphorus source which is sufficiently deficient in carbon and nitrogen and which causes increased in-situ biomass production at depths of penetration where plugging is most desirable is extremely beneficial in the practice of the above method. The inventive use of organic phosphates as the phosphorus source results in an unexpected increase in microbial activity at desired plugging sites due to the ability of the organic phosphate to be easily transported and to maintain a high thermal stability.
The term organic phosphate as used herein, refers to any compound or mixture of compounds containing the general molecular structure of phosphoric 3~07].~
or polyphosphoric acid namely, l(~lO)3PO] , in which at least one. hydrogen atom is replaced by an organic re~idue; and n is a number from 1 to about 10.
Thus, the or~anic phosphate of the present i.nvention can either origlnate as a monophosphoric acid or a polyphosphoric acid in which the phosphoric acid residues are covalently linked e.g.
O O O
Il li !l R - O - P - O - P - O - P - OH
I
~H OH G~
The or~anic residues inc~ude but are not limited to alkyl groups, and preferrea organic residues are those having the carbon content of 1 to about 17 carbon atoms per molecule. Organic residues are l.inked to the phosphoru~ atom via an ester hond. Examples of appropriate org~nic residue.s include but are Dot limited to m~thyl, ethyl, ~utyl, carbohydrates, proteins, p~ptides and lipids.
The carbon source to be used in combination with an organic phosphate phosphorus source should be in a substantially phospllorus-nutrierlt-free solutiorl, Also, the or~anic phosphflte should be in a substantia'lly carbon-nutrient-free solution, i.e., a solution sufficiently defici~,nt in carbon to render it unusable as a carbon source by the targeted microorganisms. This is to avoid achieving a complete nutrient combination and thus micr~.>b,.al actl~ity prior to locating the nutrients i.n a positi.on in the subterra.nean formation where m.icrob.'al acti~rity i~ most desired~
Therefore it is sdvarltageous to first iniect a phosphorus solution of organic phosphate which is more reAdi~y ret~.ned in the su~terranean formatior~ and 3307lCA
7 2109~77 thereafter inject a substantially phosphorus-nutrient-free carbon solution.
This permits deep penetration of the phosphorus prior to the injection of the carbon source which has less retainability in the subterranean formation. The carbon nutrient solution, being substantially phosphorus free will ultimately catch up to the previously injected phosphorus solution and form a complete nutrient combination deep within the subterranean formation. Microbial activity will occur where a complete nutrient combination exists and thus where such activity is most desired. Such method is well suited for enhancing oil recovery from oil-bearing subterranean formations.
The following example has been provided merely to illustrate the practice of the invention and should not be read as to limit the scope of the invention or the appended claims in any way.
EXAMPLES
Example I
Three screening criteria were used to determine the preferred use of organic phosphates vs. inorganic phosphate as sources of phosphorus for biological growth and metabolism. The criteria screened included the ability of the compound to support growth, the adsorption of the compound to rock, and the precipitation of the compound in the brine.
All tests were performed with field brine collected from a skimmer tank at the tract 5 tank battery located at the North Burbank Unit, Osage County, Oklahoma. Burbank brine is typical of many highly mineralized, oil-reservoir brines in that a large percentage of the solids are sodium and calcium salts (Table 1). The temperature of the brine under reservoir 3307lCA
8 21~9477 conditions is between 40 and 45C which is moderate for many oil reservoirs.
Brine samples were collected in glass bottles pre-incubated in an anaerobic glove box to remove oxygen. Bottles were capped with a butyl rubber septum.
The septum was penetrated with a 22 gauge hypodermic needle attached to a 1/4 inch (ID) nylon tubing that was used to transmit the brine sample into the bottle. Bottles of brine were transported back to the lab the same day and placed in the anaerobic glove box.
Table l Chemical Analysis of Injection Brine from the Tract 5 Tank Battery at the North Burbank Unit Analyte Concentration (g/L) ammonium .033 nitrate <.005 nitrate <.005 sulfate .020 phosphate <.050 total organic carbon .025 calcium 6.290 barium .755 magnesium 1.250 sodium 31.000 chloride 63.000 iron .0168 total dissolved solids127.300 Adsorption Screen Brine was filtered through a 0.22 micron membrane filter and enough organic phosphate ester (OP~) compound added to the brine to get a final phosphorus concentration of approximately 100 mg/L. This solution was added to a serum bottle containing 1 gram of crushed and sieved Burbank rock. The bottle was stoppered with a butyl rubber stopper and placed on a New Brunswick orbital shaker-incubator at 40C. In a like manner, sodium trimetaphosphate 3307lCA
9 2109~77 (STMP), an inorganic polyphosphate, was added to another bottle containing crushed rock and brine and incubated at 40C.
After 72 hours incubation the sample was filtered to remove the rock and the filtrate assayed for phosphorus. The phosphorus was detected using inductively coupled plasma analysis. The phosphorus detected in the filtrate is indicative of the amount of non-adsorbing or non-retained phosphorus compound after equilibration with the rock.
An index was established that compares the efficacy of the test OPE
to an inorganic phosphate, i.e., STMP. STMP was found to be more soluble in this brine as compared to other inorganic phosphates tested (e.g. sodium and potassium phosphates as well as pyrophosphates); however, its propensity to chemically degrade, at the temperature tested, to the highly insoluble ortho-phosphate made it an unattractive candidate. Therefore, STMP became a standard by which to gauge the effectiveness of other test compounds, that is, effective compounds would have to display properties superior STMP to in terms of adsorption or retention and chemical stability (i.e. precipitation).
The adsorption index (AI) was defined as the amount of STMP
phosphorus adsorbed by 1.0 gram of rock at 40C divided by the amount of OPE
adsorbed per gram of rock at 40C. An AI greater than 1.0 indicates the test compound relative to STMP is superior in terms of its inability to be retained by the rock. Subsequently, all compounds that were retained less than STMP
were considered preferred candidates for transport through the rock matrix.
As can be seen in Table 2, all OPEs tested had AIs greater than 1Ø
Precipitation Screen Samples were prepared as above for the adsorption screen except that no crushed rock was present in the bottles and the samples were held at 40C
for 23 days instead of 3 days. The long term precipitation index (LTPI) is 3307lCA
lO 2109477 defined as the weight of dissolved phosphorus in the brine after 23 days divided by the weight of dissolved phosphorus in deionized water after 3 days at room temperature. The LTPI is a measure of the chemical stability of the test compounds. Those compounds that are less likely to precipitate in brine at the higher temperature are those that have LPTIs close to 1Ø Table 2 shows that all the OPEs tested has LTPIs close to 1.0 and greater than that for STMP. For the purposes of this screen all compounds with LPTIs greater than STMP were considered to be superior and thus preferred compounds.
Table 2 Adsorption and Long Term Precipitation Indices for Various Organic Phosphate Esters Organic phosphate ester Source AI LTPI
Triethylphosphate Kodak 13.0 0.86 Methyl acid phosphate Albright-Wilson 31.0 1.05 Dimethyl acid pyrophosphate Albright-Wilson 1.08 0.88 Ethyl acid phosphate Akzo 5.40 0.97 Butyl acid phosphate Akzo 1.20 1.01 Monomethylphosphate Sigma 65.0 0.90 Sodium Trimetaphosphate Monsanto 1.0 0.64 Biological Screen These screens were performed by adding 100 mL of unfiltered Burbank brine to sterile, 120 mL serum bottles. Additions were made in an anaerobic glove box to prevent contamination by oxygen. Glucose was added at a final concentration of 0.1 percent and a phosphorus compound added at a final concentration of 100 micromolar, as phosphorus. The bottles were stoppered 3307lCA
with butyl rubber stoppers and incubated at 45C for two weeks. After incubation, the bo-ttles were sampled and bacterial numbers determined as acridine orange direct counts (AODC). In addition, the pH of the sample was measured. A lowering of pH along with an increase in cell count is indicative of bacterial fermentation of the glucose. The phosphorus compound was considered to support growth if it could stimulate an increase in bacterial numbers and lower pH to levels comparable to that obtained by using glucose plus STMP. The results in Table 3 show that four OPE supported growth and pH
declines similar to that of STMP. Therefore OPEs can better serve as effective phosphorus sources for biological growth when compared to the more commonly used inorganic phosphates.
Table 3 Comparison of the Ability of Organic Phosphate Esters vs.
Inorganic Phosphate to Support Growth of Bacteria in Burbank Brine after two Weeks Incubation at 45C
Phosphate ester Source pH AODC (X 108) bacteria/mL
Sodium Trimetaphosphate Monsanto 5.0 1.5 Alpha-glycerophosphate Sigma 5.0 2.9 Monomethyl phosphate Sigma 5.05 1.2 Ethyl acid phosphate Akzo 5.1 1.85 Methyl acid phosphate Albright-Wilson 5.05 0.62 Sodium Trimetaphosphateb Sigma 5.0 0.86 NOTE: Controls without a phosphorus source had average pH values of 6.1 and AODCs of .02 X 108 bacteria/mL.
, averages for two replicates; a, rbsults obtained with the same batch ofbrine collected on May 11, 1990; , results obtained with the same batch of brine collected on August 13, 1990.
Claims (9)
1. A process for sustaining microbial activity in subterranean formations which comprises introducing as a microbial nutrient an organic phosphate.
2. In a process of injecting microbial nutrients into a subter-ranean formation comprising the step of sequentially injecting sources of individual nutrient components which are deficient in said subterranean formation, the improvement which comprises using as a phosphorus source, an organic phosphate.
3. In a process for sustaining microbial activity in subterran-ean formations comprising the steps of injecting a substantially carbon-nutrient-free first nutrient solution comprising a phosphorus nutrient source into said subterranean formation; and thereafter, injecting a sub-stantially phosphorus-nutrient-free second nutrient solution comprising a carbon nutrient source into said subterranean formation, the improvement which comprises using as said phosphorus nutrient source an organic phos-phate.
4. The process of claim 3 wherein said organic phosphate is a monophosphoric acid of the general formula (HO)3PO in which at least one hydrogen atom is replaced by an organic residue selected from an alkyl group.
5. The process of claim 3 wherein said organic phosphate is a polyphosphoric acid of the general formula [(HO)3PO]n in which at least one hydrogen atom is replaced by an organic residue selected from an alkyl group and n is a number from about 1 to about 10.
6. The process of claim 5 wherein said polyphosphoric acid has the general formula [(HO)3PO]n and n is a number from 1 to about 10.
7. The process of claim 4 wherein said alkyl organic residue is selected from the group consisting of those alkyl organic residues having from 1 to 17 carbon atoms per molecule.
8. The process of claim 5 wherein said alkyl organic residue is selected from the group consisting of those alkyl organic residues having from 1 to about 17 carbon atoms per molecule.
9. The process of claim 1 wherein said subterranean formation is an oil-bearing subterranean formation and said process is used to enhance oil recovery.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/995,278 US5360064A (en) | 1992-12-22 | 1992-12-22 | Injection of organic phosphates for subterranean microbial processes |
| US07/995,278 | 1992-12-22 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2109477A1 CA2109477A1 (en) | 1994-06-23 |
| CA2109477C true CA2109477C (en) | 1996-12-03 |
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|---|---|---|---|
| CA002109477A Expired - Fee Related CA2109477C (en) | 1992-12-22 | 1993-10-28 | Injection of organic phosphates for subterranean microbial processes |
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| US (1) | US5360064A (en) |
| AU (1) | AU660569B2 (en) |
| CA (1) | CA2109477C (en) |
| GB (1) | GB2273727B (en) |
| NO (1) | NO304039B1 (en) |
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| GB9926157D0 (en) * | 1999-11-04 | 2000-01-12 | Norske Stats Oljeselskap | Method of microbial enhanced oil recovery |
| US6543535B2 (en) | 2000-03-15 | 2003-04-08 | Exxonmobil Upstream Research Company | Process for stimulating microbial activity in a hydrocarbon-bearing, subterranean formation |
| CA2565980A1 (en) | 2004-05-12 | 2005-12-01 | Luca Technologies, Llc | Generation of hydrogen from hydrocarbon-bearing materials |
| US20060223160A1 (en) * | 2005-04-05 | 2006-10-05 | Luca Technologies, Llc | Systems and methods for the isolation and identification of microorganisms from hydrocarbon deposits |
| US20060223159A1 (en) * | 2005-04-05 | 2006-10-05 | Luca Technologies, Llc | Generation of materials with enhanced hydrogen content from microbial consortia including thermotoga |
| US7906304B2 (en) * | 2005-04-05 | 2011-03-15 | Geosynfuels, Llc | Method and bioreactor for producing synfuel from carbonaceous material |
| US7426960B2 (en) | 2005-05-03 | 2008-09-23 | Luca Technologies, Inc. | Biogenic fuel gas generation in geologic hydrocarbon deposits |
| CN1995694B (en) * | 2006-01-06 | 2011-01-12 | 中国石油天然气股份有限公司 | A kind of oil displacement method of injecting sewage into original microorganism |
| US7416879B2 (en) | 2006-01-11 | 2008-08-26 | Luca Technologies, Inc. | Thermacetogenium phaeum consortium for the production of materials with enhanced hydrogen content |
| US7977282B2 (en) | 2006-04-05 | 2011-07-12 | Luca Technologies, Inc. | Chemical amendments for the stimulation of biogenic gas generation in deposits of carbonaceous material |
| US7696132B2 (en) * | 2006-04-05 | 2010-04-13 | Luca Technologies, Inc. | Chemical amendments for the stimulation of biogenic gas generation in deposits of carbonaceous material |
| US8479813B2 (en) | 2009-12-16 | 2013-07-09 | Luca Technologies, Inc. | Biogenic fuel gas generation in geologic hydrocarbon deposits |
| US8720546B2 (en) * | 2010-11-01 | 2014-05-13 | E I Du Pont De Nemours And Company | Prevention of biomass aggregation at injection wells |
| US8826975B2 (en) | 2011-04-12 | 2014-09-09 | Glori Energy Inc. | Systems and methods of microbial enhanced oil recovery |
| US8783345B2 (en) | 2011-06-22 | 2014-07-22 | Glori Energy Inc. | Microbial enhanced oil recovery delivery systems and methods |
| US9004162B2 (en) | 2012-03-23 | 2015-04-14 | Transworld Technologies Inc. | Methods of stimulating acetoclastic methanogenesis in subterranean deposits of carbonaceous material |
| CN105156087B (en) * | 2015-09-28 | 2018-02-16 | 中国石油化工股份有限公司 | A kind of method that oil recovery factor is improved using guanidine glue class fracturing outlet liquid |
| US12416024B2 (en) | 2018-03-29 | 2025-09-16 | Transworld Technologies Inc. | Biologically enhanced oil recovery methods |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| US3032472A (en) * | 1960-06-16 | 1962-05-01 | Phillips Petroleum Co | Microbiological secondary recovery |
| US4450908A (en) * | 1982-04-30 | 1984-05-29 | Phillips Petroleum Company | Enhanced oil recovery process using microorganisms |
| US4460043A (en) * | 1982-08-05 | 1984-07-17 | Nova/Husky Research Corporation Ltd. | Method of enhancing oil recovery by use of exopolymer producing microorganisms |
| US4475590A (en) * | 1982-12-13 | 1984-10-09 | The Standard Oil Company | Method for increasing oil recovery |
| US4522261A (en) * | 1983-04-05 | 1985-06-11 | The Board Of Regents For The University Of Oklahoma | Biosurfactant and enhanced oil recovery |
| US4558739A (en) * | 1983-04-05 | 1985-12-17 | The Board Of Regents For The University Of Oklahoma | Situ microbial plugging process for subterranean formations |
| US4534412A (en) * | 1983-12-09 | 1985-08-13 | Union Oil Company Of California | Continuous permeability reduction in subterranean reservoirs |
| US4552217A (en) * | 1984-07-09 | 1985-11-12 | Phillips Petroleum Company | Microbiocidal anionic sequesterants with polyvalent metal cations for permeability correction process |
| US4732680A (en) * | 1985-05-08 | 1988-03-22 | Betz Laboratories, Inc. | Biochemical conversion processes |
| US4610302A (en) * | 1985-07-03 | 1986-09-09 | Phillips Petroleum Company | Oil recovery processes |
| US4799545A (en) * | 1987-03-06 | 1989-01-24 | Chevron Research Company | Bacteria and its use in a microbial profile modification process |
| US4906575A (en) * | 1987-03-06 | 1990-03-06 | Chevron Research Company | Phosphate compound that is used in a microbial profile modification process |
| US4947932A (en) * | 1987-03-06 | 1990-08-14 | Chevron Research Company | Phosphate compound that is used in a microbial profile modification process |
| US4800959A (en) * | 1987-11-19 | 1989-01-31 | Alberta Oil Sands Technology And Research Authority | Microbial process for selectively plugging a subterranean formation |
| US4971151A (en) * | 1988-04-19 | 1990-11-20 | B.W.N. Live-Oil Pty. Ltd. | Recovery of oil from oil reservoirs |
| US4905761A (en) * | 1988-07-29 | 1990-03-06 | Iit Research Institute | Microbial enhanced oil recovery and compositions therefor |
| US4991652A (en) * | 1988-12-12 | 1991-02-12 | Mobil Oil Corporation | Oil reservoir permeability profile control with crosslinked welan gum biopolymers |
| US4979564A (en) * | 1989-01-31 | 1990-12-25 | The Standard Oil Company | Method of enhanced oil recovery using low tension viscous waterflood |
| US4941533A (en) * | 1989-05-16 | 1990-07-17 | The University Of Kansas | Subterranean permeability modification by using microbial polysaccharide polymers |
| US5083611A (en) * | 1991-01-18 | 1992-01-28 | Phillips Petroleum Company | Nutrient injection method for subterranean microbial processes |
| US5368099A (en) * | 1992-11-04 | 1994-11-29 | Phillips Petroleum Company | Injection of dextrins for subterranean microbial processes |
-
1992
- 1992-12-22 US US07/995,278 patent/US5360064A/en not_active Expired - Lifetime
-
1993
- 1993-10-28 CA CA002109477A patent/CA2109477C/en not_active Expired - Fee Related
- 1993-12-10 AU AU52344/93A patent/AU660569B2/en not_active Expired
- 1993-12-21 GB GB9326003A patent/GB2273727B/en not_active Expired - Lifetime
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| AU660569B2 (en) | 1995-06-29 |
| NO304039B1 (en) | 1998-10-12 |
| NO934746D0 (en) | 1993-12-21 |
| GB9326003D0 (en) | 1994-02-23 |
| CA2109477A1 (en) | 1994-06-23 |
| US5360064A (en) | 1994-11-01 |
| GB2273727B (en) | 1996-07-24 |
| NO934746L (en) | 1994-06-23 |
| AU5234493A (en) | 1994-07-14 |
| GB2273727A (en) | 1994-06-29 |
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| Bryant | Screening criteria for microbial for processes | |
| Grula et al. | Oil displacement by anaerobic and facultatively anaerobic bacteria | |
| Brown et al. | Augmenting a Microbial Selective Plugging Technique with Polymer Flooding to Increase the Efficiency of Oil Recovery-A Search for Synergy |
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