US2731090A - Petroleum production in oil bearing formations - Google Patents
Petroleum production in oil bearing formations Download PDFInfo
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- US2731090A US2731090A US213198A US21319851A US2731090A US 2731090 A US2731090 A US 2731090A US 213198 A US213198 A US 213198A US 21319851 A US21319851 A US 21319851A US 2731090 A US2731090 A US 2731090A
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- 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
- C09K8/845—Compositions based on water or polar solvents containing inorganic compounds
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- the present iriyentioncontemplates excluding water production andkirnultaneously' i cflectingia: substantial increase in the rate" of; hydrocarbon productionby'ine jecting into the formation az-jluentwetting phase"which 1s, readily miscible withformationfwaterand' which, after a predetermined time; sets r'up" as," a solid' or”relati'vely' immobile. phase.
- The; settable *w'etting' ph'ase is caused 'to substitute itself for the. wetting gp'hase' of .connate 'fo'rma-.
- the present inventiomi.onitheotherihand contemplates. sealing the minute water: capillaries without blocking orf impairing the free flow ofoiifthtouglithe:relativel'ylargerf oilconducting poresJ'.
- liquidi' preferably oiif' oiffinje'ction is 'continuedito: force the sub'stit'ute wetting phasefinto the" capillaryiinterstices. normally occupied; by :th'e'*-connate.. water" of 'ii the .forma-', tion;- the excessjmovinggalieadffofithe .oiI"..'fibw:and'pro'-, S Y ring'-theportions*oftlieformatiorradial 1y ice is manifestly important that .thevolume of oil injectiontbe;
- decreasing the water saturation increases the effective cross-section, of the passages' available for flow of the non-wettingoil phase thus increasingoil saturation and materially improving permeability of therformation to-
- The-present invention therefore *has' the advantage not only of selectivelyand exclusively; blocking water production; butofimaterially 'facili'tating oil production, by increasing: oil permeability r of r the formation.
- the w of 9 oil into the well bore' is" substantially; in-. creased," either in'th'e absence of ⁇ or at. a substantially de-' creased production of water;
- the naturrofthe present inventionv may be better.
- the" formation is lower than thenormal formation oil.
- the excess settable phase is not only forced out of the formation as indicated above but the Wetting phase tends to be forced further into the minute capillary interstices.
- the dotted line 6 in Figure 3 represents the oilwater interface location in a typical formation under normal conditions, the application of a substantial oil.
- a wetting phase miscible with formation water and capable of setting up to a condition of substantial immobility may be mentioned the known alka line metal'silicate'amrnonium bicarbonate solutions which are of desirablylow' initial viscosity, and after a -period of time, subject to reasonable control, set up as a sol or colloidal solution.
- a solution of sodium silicate and ammonium bicarbonate after a few hours, forms a silicon hydroxide or silicic acid as a sol or colloidal solution' 'witha water solution of sodium carbonate and ammonium hydroxide as'the liquid phase.
- the colloidal solution forms, the viscosity increases rapidly until it.
- Such cements are particularly advantageous in that they remain fluid for the period of time required to effect their injection into the subsurface formation, the selective replacement of the formation water by the injected fluid, and ultimate dissipation of the excess. They are also compatible with many of the typical oil-water surface active agents. Particularly important, however, is the fact that the resulting immobilized product is substantially insoluble to both oil and water and to any wetting or non-wetting phases which may be encountered in underground subsurface formations of the present character.
- compositions having these charac teristics may be employed instead of the foregoing, in particular the class of inorganic gel-forming materials in general such, for example, as the alumina-silica gels, the iron, cobalt, nickel, tin and chromium gelatinous oxides, and the copper ferrocyanide gels.
- a dilute solution of the metal sol is hydrolyzed to effect a slow precipitation of the gel.
- hydrolysis takes place at a low rate by the use of some slowly dissociating salt such as the ammonium bicarbonate above mentioned.
- the immobilizable liquid may comprise any settable material which: (1) wets the oil a bearing formation and is miscible with the formation water, (2) is preferably a relatively low viscosity liquid prior to setting, (3) sets up after a reasonable length of time to form a substantially immobile essentially oil insoluble and water insoluble material and, (4) is not miscible with the non-setting oil' phase prior to setting. Therefore, any settable material 'or composition having these physical characteristicsmanifestly meets the requirements of the present system.
- Examples of surface active agents which materially lower the interfacial tension between oil and water are polyoxyethylene sorbitan monolaurate, polyoxyethylene stearate and'the well known class of alkyl-aryl sulfonates.
- these are merely illustrative of. the vast' field of 'known oil-water interfacial .tension depressants which, in the formation, lower the capillary lifting force and result in substantial reduction of water saturation in the formation.
- small, effective quantitles is meant that quantity of the selected surface active agent which is effective to cause a material decrease in the interfacial tension' between the oil and water. This is obviously dependent upon the agent selected and is a characteristic thereof, which, per se, forms no part of the present invention. It is important to note, however, that the desired water desaturation takes place exclusively as the result of the change effected at the interface between the wetting and non-wetting phase.
- the surface active agent is only necessary to effect the disposition of the surface active agent at the interface and accordingly, instead of mixing the surface active agent with the settable phase, a small amount may be injected following injection of the settable phase, Alternatively, the surface active agent may be associated 'with the subsequently injected oil. Also a small injection of surface active agent may precede the injection of the settable phase. In each instance, the surface activeagent is preferably employed in solution and in a quantity sufiicient to' thoroughly permeate the interface.
- the well in question extends into the Oligocene Reservoirin the Manvel Field, in Brazoria County, Texas.
- the well depth is about 5,000 ft. and 'thepliysical properties of the producing formation involve aporosity of about 25% and a permeability of a'bout 1000 millidarcys,
- the well, prior to treatment produced about 60 barrels per day of oil and 40 barrels per day of water at a drawdown of about 10 p. s. i. in a production zone about 10 ft. thick.
- a settable fluid is prepared by mixing about 50 parts of 18% sodium silicate and 15 parts of 12% ammonia bicarbonate solution and adding about 35 parts of water. Production from the well is stopped and about 150 barrels of this solution is forced through the well bore out into the formation. This injection is immediately followed by the injection of 450 barrels of oil containing about of Atlas 6-931 comprising a polyoxyethylene-cottonseed oil reaction product, a known surface-active agent which is radically effective in reducing the interfacial tension between oil and water.
- the oil injection forces the aqueous, substitute setting phase into the smaller water bearing capillaries and simultaneously displaces any excess outwardly into the formation, opening the larger and normally oil beating spaces for oil flow.
- the well is left shut in for approximately 24 hours to permit solidification or immobilization of the settable phase.
- the present invention is effective for selective water exclusion by selectively sealing off the water bearing capillaries about the region of production.
- the permeability of the formation to oil may be materially increased. This follows from the fact, intimated above, that the material water desaturation, resulting from the action of the surface active agent, and the pressuring of the formation with non-wetting phase, opens a much greater portion of the interior space to the flow of oil. Accordingly oil production becomes strikingly greater and the pumping of undesired water from the formation is obviated. As a result difliculties such as corrosion, inherent in the bandling of ground waters, are obviated.
- shutting in of the well after clearing excess settable phase from the oil bearing passages is held for a period of time sufficient to permit immobilization of the setting phase. Manifestly this will vary with the setting time of the composition selected.
- the present invention contemplates resort to any suitable formation pressuring practice in accomplishing this result.
- Such technique forms, per se, no part of the invention.
- it may involve, for example, pumping of oil into the formation during the setting period at a rate suflicient to maintain the desired increment in pressure over that of the normal formation pressure.
- a method according to claim 1 wherein said formation in said region undergoing treatment is treated with a surface active agent to materially lower in the interfacial tension at the interface between the aqueous liquid and said second liquid.
Description
Jan. 17, 1956 R. w. JOHNSTON, JR 2,731,090
PETROLEUM PRODUCTION IN OIL BEARING FORMATIONS Filed Feb. 28, 1951 INVENTOR.
I BY/Pwp/V; o/l/vsTo/tgzfe.
United States Patent 6) 1 131,090... PETROLEUMJRODUGHON .maom naanme,
FORMATIONSa.
Rowland W. J ohnston; ills Bkuaifg-g Tgxg i T w pa y, NwflmkaN. Y., atcor rano pe, Delaware l 4 Application ary =28,7 195 1, Serlal .No..213,198.
6'=Claims.1.- (clause-29 The. present" invention relates -to the? production of 10 petroleum hydrocarbons fronr subsurface formationsiby means of a producinggwell,and"is=more specificallycom. cernedwitlr hydrocarbbwproduction from asubsurfaceformation containinganon wettingphase ofr'liquidp'etrwleum, and awettinggmha f connate-formation water whichirises by capillaryfactinnabovethe'watertable:
Broadly; the present iriyentioncontemplates excluding water production andkirnultaneously' i cflectingia: substantial increase in the rate" of; hydrocarbon productionby'ine jecting into the formation az-jluentwetting phase"which 1s, readily miscible withformationfwaterand' which, after a predetermined time; sets r'up" as," a solid' or"relati'vely' immobile. phase. The; settable *w'etting' ph'ase is caused 'to substitute itself for the. wetting gp'hase' of .connate 'fo'rma-. tion water withoutibloeking ;the passages "of" pores'ocf cupied by the non-wetting;petroleum:qhydrocarbonz In short the. settable material fexciusively occupies ithe more minute capillaries previouslyjoccupiedby the formation water and, upon setting; positively; blocks thejcapillary new of formation wateririn :the *region. of 'the'welLfborer.
It is particularly j important to distinguish? the .Piesent invention from prior proposals which have been advanced to inject into. the formation asmatcrial "which-sets up'as, a" solid to bl'ock'the formation 'oria portionthereofi Such. proposals usually look"toward'the-creation-'ofia solid claim or dike through some predetermin'etlfsectiou"ofjthe forum-- tion for the purpose of preyenting all"fiow'in' that region;;.-
The present inventiomi.onitheotherihand, contemplates. sealing the minute water: capillaries without blocking orf impairing the free flow ofoiifthtouglithe:relativel'ylargerf oilconducting poresJ'. Asiaresult'ioil diowiisfunimpairedz' by capillary water migratingintoitspatlrof flow and'the substitute iwettin'g phaS8,f"i$, in: effect'gflimmobilized' inthe capillaryinterstices so 'tliatifdesmot move'into thepath" of oil flow toirestrictfoil. permeabilityandtoresultin' water'productiom Therefore, blockin'g oruamming,ipf'i the formation as hitherto proposed would beffatai to the-present invention. and it'is'important that itbe avoldedi;
To this end the"substitute wetting-phase?capab'le'of setting up" in 'a condition of'isub'stantial immobi1ity 'is"in'-.,- jected through the well bore 'it'ittfthezformation preferably asa readily fluent liquid"anid"is'cause'dutr radially flow a substantial distance outwardlyjftprn the'well bore: Asfa' result a portion of the fdrmationoif "is displaced and the e substitute wettingphase; Heingjn' excessiof. normal wetting phase saturation; itendsfto' drain into 'the-wettedcapil laries normally occupied byjthe"connate-formation water;
After thuscompletin' F 'ieCtion' ofthei substitute.- im-" mobi-lizable liquid into za predeterminedi"sectioni of Tithe formation about the :well' there andibefore setting has cornmenced, the excess ofi'tlfe immobilizableili'quid ,over and, above that which will'iibe-"receiyedby the? water. containing' capillaries must bedisplaced"'andremoved' from the. oil containing passages. A convenient v,way of accomplish ing the result" is: .to' positively inject into thee formation about the well'bore asubstantithvolumeof'ianou=wetting. liquidi' preferably oiif' oiffinje'ction is 'continuedito: force the sub'stit'ute wetting phasefinto the" capillaryiinterstices. normally occupied; by :th'e'*-connate.. water" of 'ii the .forma-', tion;- the excessjmovinggalieadffofithe .oiI"..'fibw:and'pro'-, S Y ring'-theportions*oftlieformatiorradial 1y ice is manifestly important that .thevolume of oil injectiontbe;
sufficient to restore' the original and preferably the maxi-- mum oili saturation throughout the entire section ofith'e' formation which is subjected to treatment.
Another important feature of the present invention'involves -treating' the interface between substitute wetting, phase' and the 1oil witha surface active agent effective to substantially reduce the interfacialjtension between .theoil and wetting phase-and thereby materially reduce the water saturation of the formation under treatment; Manifestly, decreasing the water saturation" increases the effective cross-section, of the passages' available for flow of the non-wettingoil phase thus increasingoil saturation and materially improving permeability of therformation to- The-present invention therefore *has' the advantage not only of selectivelyand exclusively; blocking water production; butofimaterially 'facili'tating oil production, by increasing: oil permeability r of r the formation. In short, the w of 9 oil into the well bore' is" substantially; in-. creased," either in'th'e absence of {or at. a substantially de-' creased production of water;
The naturrofthe present inventionv may be better.
understood byreference to accompanying drawing,,,off.
WhichQFigure-"I represents, inidiagrammatic or symbolic form;- a crossrsectiom; highly magnified, takenthrough. a typicalfloil bearing'formation. The'z-solidgrains. ofQth'e formation are represented by the numeral", 1 and these; as: indicated, leave between. them' minute pores of" irregu lar j cross" sectional configuration. The wetting, phase: of connate" water occupies the' more restricted portions: of" the pores at" 2, risingupwardlyin these, minute capillaries by. capillary attraction from the water table,-- more or; less diagrammatically represented. by thevline marked Water table? a distance it. Thenon wetting phase of-oil accordingly occupies the larger pase sagesof-the poresas, indicatedby the reference numeral}. Under normal, static conditions; the pressure, in, the.
water-at the-interface between the oil and iwaterisnecesa. S3111)" less than; the pressure at the surface. of the.;.water table "by anamount equal tothe head..of.,waterabove the water table. This .,is in turn dependent, upon the. height.
of the: point: of reference above the water table. andthe. density' ofthe'formation water.
Likewise, atthe oil-water interface, the oil-.-p1 'essure.is.
less, than thepressure at the water table, byraniamount equal to the headof oil abovethe water table. But, since...
thedensity'ofthewater. or wettingphase .is substantially greatertliarr the density offthe oil phase, .the. oilapres'sure;
at any poinrofreference is substantially, greater..,than,the. water-pressure: This ditfe'rential'is the capillary pressure Ifithepressurelin" the. well at thepoiutwhere it meets.
the" formation is lower than thenormal formation oil.
pressure; then oil will tend to. flow fromtheformationmto-thewell. The difference in. these two. pressuresis called .drawado'wnf? If the. draw.-down;;is., suflicient;.to,.
brirrggthe pressure in thewellbore :below thestatie water,-
pressure, then both water and .oil' will,.;tend..,to flowinto.
the well;
Moreov'en as vpdrawaiovvn imposedupontthe formae. tion, both the oil andwater pressures in the vicinity of the well bore necessarily tend to approach the same pressure, namely that resulting from the draw-down.
In any event, however, as draw-down is imposed upon the well, the resultant release in pressure in the adjacent oil phase permits the capillary wetting phase to move outwardly into the oil-bearing passages, for example, to a point indicated by the dotted lines 4. This manifestly tends to restrict the cross sectional area of the oilpassages and accordingly the fiow of oil. Moreover, as the pressure on the liquid phases in the formation becomes further reduced due to an increase in draw-down, water moves further out into the oil passages and ultimately proceeds through the pores and is produced with the oil.
The results realized by the practice of the present invention are represented on a similar diagrammatic scale in Figure 2 of the present drawing wherein the capillary wetting phase of water which normally occupies the rela tively restricted pores is substituted by an immobile wetting phase which, after introduction into the capillaries normally occupied by the water, sets up or immobilizes to form a selective water barrier. By virtue of its wetting character, the immobilizable liquid injected into the formation moves into the region previously occupied by the formation water to the position indicated diagrammatically by the reference numeral 5.
If the formation is subjected to treatment with oil under a pressure substantially in excess of normal formation oil pressure, and before the wetting phase sets up, the excess settable phase is not only forced out of the formation as indicated above but the Wetting phase tends to be forced further into the minute capillary interstices. For example, if the dotted line 6 in Figure 3 represents the oilwater interface location in a typical formation under normal conditions, the application of a substantial oil.
f Essentially, the same effect, as the last mentioned, re-
sults from the inclusion of the surface active agent effective to materially lower the interfacial tension between the wetting and non-wetting phases. Inclusion of an effective portion of such an agent with the immobilizable wetting phase has the effect of lowering the capillary force tending to cause water to rise in the formation.
This follows because of the fact that in any formation of fixed internal porosity the capillary force acting upon the water is dependent upon the interfacial tension between the wetting and non-Wetting phases and the angle at which the Wetting phase wets the solid surfaces of the formation. Therefore, reduction of the oil-Water surface tension at this interface lowers the capillary lifting force and results in a tendency for decreased saturation of the formation by water as well as a correspondingly increased saturation by oil wtih resulting improvement in oil permeability.
As examples of a wetting phase miscible with formation water and capable of setting up to a condition of substantial immobility may be mentioned the known alka line metal'silicate'amrnonium bicarbonate solutions which are of desirablylow' initial viscosity, and after a -period of time, subject to reasonable control, set up as a sol or colloidal solution. Thus, a solution of sodium silicate and ammonium bicarbonate, after a few hours, forms a silicon hydroxide or silicic acid as a sol or colloidal solution' 'witha water solution of sodium carbonate and ammonium hydroxide as'the liquid phase. As the colloidal solution forms, the viscosity increases rapidly until it.
becomes a semi-solid. On further standing, it becomes an elastic gel of high molecular weight and subsequently ecomes more rigid and increasingly inelastic.
Such cements are particularly advantageous in that they remain fluid for the period of time required to effect their injection into the subsurface formation, the selective replacement of the formation water by the injected fluid, and ultimate dissipation of the excess. They are also compatible with many of the typical oil-water surface active agents. Particularly important, however, is the fact that the resulting immobilized product is substantially insoluble to both oil and water and to any wetting or non-wetting phases which may be encountered in underground subsurface formations of the present character.
Many other settable compositions having these charac teristics may be employed instead of the foregoing, in particular the class of inorganic gel-forming materials in general such, for example, as the alumina-silica gels, the iron, cobalt, nickel, tin and chromium gelatinous oxides, and the copper ferrocyanide gels.
The mechanism of gel formation per se forms no part of the present invention and accordingly will not be described in detail. In general, however, a dilute solution of the metal sol is hydrolyzed to effect a slow precipitation of the gel. Preferably, as in the case of the first illustrated example, hydrolysis takes place at a low rate by the use of some slowly dissociating salt such as the ammonium bicarbonate above mentioned.
In general, however, the immobilizable liquid may comprise any settable material which: (1) wets the oil a bearing formation and is miscible with the formation water, (2) is preferably a relatively low viscosity liquid prior to setting, (3) sets up after a reasonable length of time to form a substantially immobile essentially oil insoluble and water insoluble material and, (4) is not miscible with the non-setting oil' phase prior to setting. Therefore, any settable material 'or composition having these physical characteristicsmanifestly meets the requirements of the present system.
Examples of surface active agents which materially lower the interfacial tension between oil and water are polyoxyethylene sorbitan monolaurate, polyoxyethylene stearate and'the well known class of alkyl-aryl sulfonates. However, as above intimated, these are merely illustrative of. the vast' field of 'known oil-water interfacial .tension depressants which, in the formation, lower the capillary lifting force and result in substantial reduction of water saturation in the formation.
Small effective quantities of these agents may advantageously be dissolved in the settable phase prior to introduction into the formation. By small, effective quantitles is meant that quantity of the selected surface active agent which is effective to cause a material decrease in the interfacial tension' between the oil and water. This is obviously dependent upon the agent selected and is a characteristic thereof, which, per se, forms no part of the present invention. It is important to note, however, that the desired water desaturation takes place exclusively as the result of the change effected at the interface between the wetting and non-wetting phase. Therefore, it is only necessary to effect the disposition of the surface active agent at the interface and accordingly, instead of mixing the surface active agent with the settable phase, a small amount may be injected following injection of the settable phase, Alternatively, the surface active agent may be associated 'with the subsequently injected oil. Also a small injection of surface active agent may precede the injection of the settable phase. In each instance, the surface activeagent is preferably employed in solution and in a quantity sufiicient to' thoroughly permeate the interface.
Following is an illustrative example of the application of the present invention to as producing oil well. The well in question extends into the Oligocene Reservoirin the Manvel Field, in Brazoria County, Texas. The well depth is about 5,000 ft. and 'thepliysical properties of the producing formation involve aporosity of about 25% and a permeability of a'bout 1000 millidarcys, The well, prior to treatment, produced about 60 barrels per day of oil and 40 barrels per day of water at a drawdown of about 10 p. s. i. in a production zone about 10 ft. thick.
In accordance with this practice of the present invention, a settable fluid is prepared by mixing about 50 parts of 18% sodium silicate and 15 parts of 12% ammonia bicarbonate solution and adding about 35 parts of water. Production from the well is stopped and about 150 barrels of this solution is forced through the well bore out into the formation. This injection is immediately followed by the injection of 450 barrels of oil containing about of Atlas 6-931 comprising a polyoxyethylene-cottonseed oil reaction product, a known surface-active agent which is radically effective in reducing the interfacial tension between oil and water.
The oil injection forces the aqueous, substitute setting phase into the smaller water bearing capillaries and simultaneously displaces any excess outwardly into the formation, opening the larger and normally oil beating spaces for oil flow. The well is left shut in for approximately 24 hours to permit solidification or immobilization of the settable phase.
Thereafter production from the well is resumed at a substantially increased permeability. For example, at a drawdown of 10 p. s. i., the well now produces about 90 barrels per day of oil with no water production. At a drawdown of p. s. i., the oil production rises to approximately 130 barrels per day with no water production.
From the foregoing, it is apparent that the present invention is effective for selective water exclusion by selectively sealing off the water bearing capillaries about the region of production. ln addition the permeability of the formation to oil may be materially increased. This follows from the fact, intimated above, that the material water desaturation, resulting from the action of the surface active agent, and the pressuring of the formation with non-wetting phase, opens a much greater portion of the interior space to the flow of oil. Accordingly oil production becomes strikingly greater and the pumping of undesired water from the formation is obviated. As a result difliculties such as corrosion, inherent in the bandling of ground waters, are obviated.
As above indicated, the shutting in of the well after clearing excess settable phase from the oil bearing passages is held for a period of time sufficient to permit immobilization of the setting phase. Manifestly this will vary with the setting time of the composition selected.
As also intimated, it is advantageous during the setting period to maintain upon the formation a pressure substantially in excess of normal formation pressure to positively force the wetting phase of settable material back into the minute water wet capillaries, thereby correspondingly increasing the effective cross sectional area of the oil-bearing passages and materially improving oil permeability.
The present invention contemplates resort to any suitable formation pressuring practice in accomplishing this result. Such technique forms, per se, no part of the invention. However, it may involve, for example, pumping of oil into the formation during the setting period at a rate suflicient to maintain the desired increment in pressure over that of the normal formation pressure.
It is important to note that the advantages of the present invention may be fully realized even though the for mation is treated to only a relatively limited extent about the well bore. This follows from the fact that in a porous radial flow system the pressure drop at the central point of withdrawal in the well bore is reflected materially only a relatively short distance out into the formation. In other words the pressure drop is concentrated close to the well. Thus, for example, the pressure drop is greatest in regions close to the well bore and radically decreases in regions outwardly therefrom. As a result treatment for a distance greater than 50-100 radial feet is seldom justifled. Actually treatment for as little as 10 radial feet is normally of considerable advantage although radial treatments to the extent of 25 radial feet are to be preferred.
Obviously many modifications and variations of the invention, as hereinbefore set forth, 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:
l. A method of producing petroleum from a well bore penetrating a porous subsurface petroleum-producing formation which formation immediately overlies a water table, the capillaries of said formation being occupied by a non-wetting liquid oil phase and a liquid phase of connate capillary formation water derived by capillary attraction from said water table, which formation water wets the surfaces of the capillaries of said formation, which comprises injecting from said well bore into the capillaries of said formation a fluent aqueous liquid capable of setting up, per se, to a solid, said aqueous liquid wetting the surfaces of the capillaries of said formation and being miscible with said capillary formation water and immiscible with said liquid oil phase contained in the capillaries of said formation, whereby said injected aqueous liquid displaces said capillary formation water from the capillaries of said formation and also some of the liquid oil phase from the normally oil-occupied portion of the capillaries for a substantial region surrounding said well bore, thereafter displacing said injected aqueous liquid out of the normally oil-occupied portion of the capillaries of said formation in said region surrounding said well bore by injecting into said formation from said well bore a second liquid which is nonwetting with respect to the surfaces of the capillaries of said formation in an amount sufficient at least to saturate the normally oil-occupied portion of the capillaries of said formation in said region undergoing treatment, said second liquid being immiscible with said aqueous liquid and miscible with said liquid oil phase contained in said capillaries, discontinuing the injection of said second liquid and permitting said injected aqueous liquid to set up to a solid within said capillaries and thereafter producing petroleum from said formation via said well bore.
2. A method in accordance with claim 1 wherein the amount of said second liquid injected into said formation is substantially in excess of the amount of said aqueous liquid injected into said formation.
3. A method in accordance with claim 1 wherein said second liquid is injected into said formation at a pressure sufficient to force said second liquid into the normally water-occupied portion of the capillaries in the region undergoing treatment thereby increasing the oil permeability of the thus-treated region of said forma tion.
4. A method according to claim 1 wherein the formation is treated for at least about 10 feet radially outwardly from the well bore.
5. A method according to claim 1 wherein said formation in said region undergoing treatment is treated with a surface active agent to materially lower in the interfacial tension at the interface between the aqueous liquid and said second liquid.
6. A method according to claim 1 wherein said second liquid is liquid oil.
References Cited in the file of this patent UNITED STATES PATENTS 2,090,626 Grebe Aug. 24, 1937 2,207,759 Reimers July 16, 1940 2,229,177 Kennedy et al Jan. 21, 1941 2,237,313 Prutton Apr. 8, 1941 2,259,875 Bent et a1. Oct. 21, 1941 2,267,855 Chamberlain Dec. 30, 1941 2,379,561 Bennett July 3, 1945 2,402,433 Munn June 18. 1946
Claims (1)
1. A METHOD OF PRODUCING PETROLEUM FROM A WELL BORE PENETRATING A POROUS SUBSURFACE PETROLEUM-PRODUCING FORMATION WHICH FORMATION IMMEDIATELY OVERLIES A WATER TABLE, THE CAPILLARIES OF SAID FORMATION BEING OCCUPIED BY A NON-WETTING LIQUID OIL PHASE AND A LIQUID PHASE OF CONNATE CAPILLARY FORMATION WATER DERIVED BY CAPILLARY ATTRACTION FROM SAID WATER TABLE, WHICH FORMATION WATER WETS THE SURFACES OF THE CAPILLARIES OF SAID FORMATION, WHICH COMPRISES INJECTING FROM SAID WELL BORE INTO THE CAPILLARIES OF SAID FORMATION A FLUENT AQUEOUS LIQUID CAPABLE OF SETTING UP, PER SE, TO SOLID, SAID AQUEOUS LIQUID WETTING THE SURFACES OF THE CAPILLARIES OF SAID FORMATION AND BEING MISCIBLE WITH SAID CAPILLARY FORMATION WATER AND IMMISCIBLE WITH SAID LIQUID OIL PHASE CONTAINED IN THE CAPILLARIES OF SAID FORMATION, WHEREBY SAID INJECTED AQUEOUS LIQUID DISPLACES SAID CAPILLARY FORMATION WATER FROM THE CAPILLARIES FOR A SUBSTANTIAL REGION SOME OF THE LIQUID OIL PHASE FROM THE NORMALLY OIL-OCCUPIED PORTION OF THE CAPILLARIES FOR A SUBSTANTIAL REGION SURROUNDING SAID WELL BORE, THEREAFTER DISPLACING SAID INJECTED AQUEOUS LIQUID OUT OF THE NORMALLY OIL-OCCUPIED PORTION OF THE CAPILLARIES OF SAID FORMATION IN SAID REGION SURROUNDING SAID WELL BORE BY INJECTING INTO SAID FORMATION FROM SAID WELL BORE A SECOND LIQUID WHICH IS NONWETTING WITH RESPECT TO THE SURFACES OF THE CAPILLARIES OF SAID FORMATION IN AN AMOUNT SUFFICIENT AT LEAST TO SATURATE THE NORMALLY OIL-OCCUPIED PORTION OF THE CAPILLARIES OF SAID FORMATION IN SAID UNDERGOING TREATMENT, SAID SECOND LIQUID BEING IMMISCIBLE WITH SAID AQUEOUS LIQUID AND MISCIBLE WITH SAID LIQUID OIL PHASE CONTAINED IN SAID CAPILLARIES, DISCONTINUING THE INJECTION OF SAID SECOND LIQUID AND PERMITTING SAID INJECTED AQUEOUS LIQUID TO SET UP TO A SOLID WITHIN SAID CAPILLARIES AND THEREAFTER PRODUCING PETROLEUM FROM SAID FORMATION VIA SAID WELL BORE.
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US213198A US2731090A (en) | 1951-02-28 | 1951-02-28 | Petroleum production in oil bearing formations |
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US213198A US2731090A (en) | 1951-02-28 | 1951-02-28 | Petroleum production in oil bearing formations |
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US2731090A true US2731090A (en) | 1956-01-17 |
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US213198A Expired - Lifetime US2731090A (en) | 1951-02-28 | 1951-02-28 | Petroleum production in oil bearing formations |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
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US2874779A (en) * | 1956-03-23 | 1959-02-24 | California Research Corp | Oil well treating method |
US3055426A (en) * | 1959-02-05 | 1962-09-25 | Jersey Prod Res Co | Method for consolidating incompetent subsurface earth zones |
US3376926A (en) * | 1967-04-18 | 1968-04-09 | Halliburton Co | Methods of placement of low ph silicic acid in carbonaceous geological formations |
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US2090626A (en) * | 1936-09-05 | 1937-08-24 | Dow Chemical Co | Method of preventing infiltration in wells |
US2207759A (en) * | 1938-08-10 | 1940-07-16 | Dow Chemical Co | Treatment of earth and rock formations |
US2229177A (en) * | 1939-05-26 | 1941-01-21 | Gulf Research Development Co | Water shutoff in oil and gas wells |
US2237313A (en) * | 1938-12-24 | 1941-04-08 | Dow Chemical Co | Method of treating well bore walls |
US2259875A (en) * | 1936-09-09 | 1941-10-21 | Shell Dev | Method of treating oil and gas wells |
US2267855A (en) * | 1937-03-15 | 1941-12-30 | Dow Chemical Co | Treatment of wells producing mineral fluid |
US2379561A (en) * | 1941-11-21 | 1945-07-03 | Continental Oil Co | Method of increasing the effective permeability of porous formations |
US2402433A (en) * | 1941-05-19 | 1946-06-18 | Chemical Service Company | Treatment of oil wells |
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1951
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Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
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US2090626A (en) * | 1936-09-05 | 1937-08-24 | Dow Chemical Co | Method of preventing infiltration in wells |
US2259875A (en) * | 1936-09-09 | 1941-10-21 | Shell Dev | Method of treating oil and gas wells |
US2267855A (en) * | 1937-03-15 | 1941-12-30 | Dow Chemical Co | Treatment of wells producing mineral fluid |
US2207759A (en) * | 1938-08-10 | 1940-07-16 | Dow Chemical Co | Treatment of earth and rock formations |
US2237313A (en) * | 1938-12-24 | 1941-04-08 | Dow Chemical Co | Method of treating well bore walls |
US2229177A (en) * | 1939-05-26 | 1941-01-21 | Gulf Research Development Co | Water shutoff in oil and gas wells |
US2402433A (en) * | 1941-05-19 | 1946-06-18 | Chemical Service Company | Treatment of oil wells |
US2379561A (en) * | 1941-11-21 | 1945-07-03 | Continental Oil Co | Method of increasing the effective permeability of porous formations |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
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US2874779A (en) * | 1956-03-23 | 1959-02-24 | California Research Corp | Oil well treating method |
US3055426A (en) * | 1959-02-05 | 1962-09-25 | Jersey Prod Res Co | Method for consolidating incompetent subsurface earth zones |
US3376926A (en) * | 1967-04-18 | 1968-04-09 | Halliburton Co | Methods of placement of low ph silicic acid in carbonaceous geological formations |
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