US2246726A - Treatment of oil wells - Google Patents

Treatment of oil wells Download PDF

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US2246726A
US2246726A US301754A US30175439A US2246726A US 2246726 A US2246726 A US 2246726A US 301754 A US301754 A US 301754A US 30175439 A US30175439 A US 30175439A US 2246726 A US2246726 A US 2246726A
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sand
oil
water
well
producing
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Allen D Garrlson
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Texaco Inc
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/60Compositions for stimulating production by acting on the underground formation
    • C09K8/84Compositions based on water or polar solvents
    • C09K8/845Compositions based on water or polar solvents containing inorganic compounds
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/58Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
    • C09K8/592Compositions used in combination with generated heat, e.g. by steam injection
    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/24Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S507/00Earth boring, well treating, and oil field chemistry
    • Y10S507/935Enhanced oil recovery

Definitions

  • This invention relates to the treatment of an oil well, and more particularly to the chemical treatment of the sand adjacent a producing well in ,order to render the sand preferentially wet;
  • My invention resides in a method of causing oil to flow through all of the capillaries and crevices of an oil producing sand by removing the water film from the walls 01 the capillaries and crevices and rendering the surfaces oil-wettable. In this manner the flow of water into the well is retarded by the same force which obstructs thev flow of oil through the average water-wet oil producing sandl
  • Vletti and Allen D.Garrison there is disclosed and claimed a method of treating a producing, sand of this character which is wet with water, by the depositing of a water and oil insoluble precipitate on thesand grains, which precipitate is of such character that it does not all or block the pore space of the sand and is preferentially wettable by oil so that the sand becomes wet with oil,'wh ereby'the proportion of oil produced by the well is increased while the proportion of water so produced is decreased.
  • the present invention constitutes 'an improvement over the method of said patent, and involves the pretreatment or the producing sand so that the pore space of the sand is enlarged or increased and the sand rendered in more suitable condition to receive the preferentially oil-wettable coating which is then'deposited upon the sand grains.
  • the producing sand is first flushed with an aqueous alkaline solution which is eflective to disperse fine, clay particles and silt from the interstices of the sand and which may also dissolve certain calcium and magnesium salts present in the formation, as well as remove oil irom the pore space.
  • This flushing treatment is then followed by a treatment to coat the sand grains with a water and oil insoluble precipitate which is preferentially oil-wettable.
  • a satisfactory aqueous flushin'g medium for carrying out the first step of this process is an aqueous alkaline solution of an alkali metal hex-ametaphosphate such as sodium hexametaphosphate, potassium hexametaphosphate, lith-' iumhexametaphosphate and ammonium hexametaphosphate.
  • an alkali metal hex-ametaphosphate such as sodium hexametaphosphate, potassium hexametaphosphate, lith-' iumhexametaphosphate and ammonium hexametaphosphate.
  • NaPOa sodium salt
  • the presence of the metaphosphate compound in the aqueous flushing medium prevents precipitation of calcium and magnesium compounds or salts which may be dissolved from the formation, by rendering these calciumand magnesium compounds immune to reaction by repressing ionization thereof. It is believed that the hexametaphosphate compound reacts with calcium and magnesium ions, forming complex compounds which are only slightly ionized and which remain in the aqueous alkaline solution. The aqueous flushing medium is thereby rendered capable of dissolving and holding in solution increased quantities of such salts, so that an effecmay be used in conjunction with the metaphosphate.
  • alkali metal salts such as sodium carbonate, sodium pyrophosphate and the like, or balanced mixtures of alkali metal hydroxides with alkali metal salts of such acids as boric, phosphoric, carbonic, oxalic,
  • silicic and similar weak acids Sufiicient buffer salt or salt mixture is added to the aqueous fiushzone.
  • suitable clay dispersing col-v loidal agents of this character are the water soluble alkali metal salts of such organic acids as tannic acid, gallic acid; humic acid, ogalllc acid and the like. A small proportion of such colloidal agent is satisfactory, for example a proportion of .01% to .5% on the basis of the aqueous flushing medium.
  • calcium sequestering agents may be employed.
  • various molecularly dehydrated phosphates such as the triphosphates, tetraphosphates and higher condensed nuclei phosphates of this character, as well as the sulfur containing derivatives thereof, such as the trithiophosphates, tetrathiophosphates, etc.
  • the nitrogenbearing complexes of the molecularly dehydrated phosphoric acids which possess calcium-sequestering action can be used. Examples of such nitrogen-bearing complexes are imidophosphoric acids, diamidophosphoric acids, phosphirnic acids and the like: 5 I
  • calcium sequestering agents are employed in aqueous solution, preferably in the presence of a suitable buifer salt or buffer salt .mixture of the character described above to maintain the aqueous fiushing medium in a slightly alkaline state, for example of a pH from 8.0 to 11.5.
  • a suitable clay dispersing colloidal agent of the character of the water soluble alkali obstruction to the flow through the pore space of the producing sand is due to clogging precipitates of calcium and magnesium compounds, or
  • any of the above mentioned ploy a calcium sequestering agent, and good re- I aqueous alkaline solutions or solutions containing a clay deflocculating agent can be combined with any of the calcium sequestering compounds capable of solvent action on the alkaline earth salts.
  • This preliminary flushing step preceding the depositing of the preferentially oil-wettable coating is of particular advantage in the case of old wells where the production rate has declined due to the cloning of the pores of the producing formation, as well as where the ratio of water to oil produced from the formation may have substantially increased.
  • a suitable aqueous alkaline solution of the character set out above is first forced into the well and into the sand adjacent the well to clean the pore space of the sand by removing the fine silt and clay and dissolving the soluble salts.
  • This treatment is also efiective to flush out oil from the pore space, so that the sand grains will be left in freely exposed and suitable condition for the subsequenttreatment of depositing the preferentially oil-wettable precipitate thereon.
  • This first treatment may be followed directly with solutions producing the desired oil-wettable precipitate, or an intermediate slug of water can be forced into the well between the first flushing treatment and the subsequent coating of the sands with the desired precipitate, or the fiushing liquid can be first removed from the sand and the well bore by pumping or bailing.
  • the prepared sand bed is then treated to coat the sand grains with a thin adhering film of a water and oil in-. soluble precipitate which is preferentially wettable by oil.
  • a solution of a precipitatable compound of the preferential wetting character described there is forced into the well and into the sand adjacent the well a solution of a precipitatable compound of the preferential wetting character described.
  • the procedure described above may be repeated one or more times, so as to secure the desired effective deposit and coating of the sand grains throughout the water-wet sand.
  • this is then followed by forcing a charge of oil into the well in order to force the chemicals farther out into the sands to increase the zone of treatment and to immediately create a zone of sand around the well which is wet by oil.
  • Suitable materials which possess the preferential wetting property include various water and oil insoluble salts of sulfonated oils, fats orfatty acids.
  • the alkaline earth and heavy metal salts including those of calcium, barium, iron, manganese, zinc, tin, lead, and the like of sulfonated oils, fats or fatty acids may be employed.
  • Natural fats such as tallow, olein, stearine and the like, which have been sulfonated by treatment with sulfuric acid, are suitable.
  • sulfonated fatty acids formed by sulfonating stearic, palmitic, oleic, and the like are included.
  • a very satisfactory and comparatively cheap material which is a by-product of the petroleum industry, is the' sulfonic sludge acid derived from the treatment of petroleum oil with sulfuric acid, and termed herein a petroleum oil sulfonate.
  • These various materials may con- ,veniently be used in the form of their alkali metal salts, whereby a water solution of the soluble salt may first be forced into the bore of the well and into the sand immediately surrounding the well. Then a water solution of a water soluble salt of calcium.
  • barium, or other alkaline earth or heavy metal, such as a chloride or nitrate, is forced into the well and into the sand to react with the first mentioned solution to produce a precipitate of the water and oil insoluble metal salt ofthe sulfonated oil, fat or fatty acid,
  • a dilute water solution of sodium hexametaphosphate buffered with sodium carbonate and also containing sodium tannate is forced into the well and the producing sand. This is followed by a water wash to remove the first flushing liquid, then a dilute water solution of the sodium salt of petroleum sulfonate is introduced into the sand, and this is followed by a wash with a dilute solution of calcium chloride. Another charge of the sodium salt of petroleum sulfonate is then forced into the well, followed by another charge of the calcium chloride solution. This may be repeated still a third time, or even more, depending upon the extent of sand to be treated. Finally a quantity of oil is pumped into the well which will force the chemicals farther out into the sand and will renderthe sand in the immediate vicinity of the well wet by oil.
  • a dilute water solution of sodium pyrophosphate is first forced into the well and agitated in the hole for a period of time with a spudder. I 'I'hisis followed by bailing to remove the first flushing liquid together with the de iiocculated clay and loosened sand carried in suspension therein.
  • the producing sand may then be dried to remove water from the pore space thereof, asby suitable chemical or other dehydrating treatment, although this step may be omitted and good results obtained in many cases.
  • a coating of the preferentially oil-wet- 'table material is then applied to the producing sand and finally 'a quantity of oil pumped into able wetting agent or surface tension depressant.
  • Any suitable wetting su ace tension depressant which is water soluble and non-reactive with the fluid, and does not form clogging precipitates with constituents of the formation can be employed, such as various alcohols, ketones, sulfonated organic detergents, and the like.
  • alkali metal salts of sulfated long chain fatty alcohols such as sodium oleyl sulfate
  • alkali metal salts oflong chain fatty acid-taurine condensation products such as sodium oleyl sulfate
  • other synthetic organic detergents of this general type whose calcium salts are water soluble.
  • any other suitable accordance with the present invention which relates to a combination of such preferential oilwetting treatment with a preliminary flushing of the sand bed such as to render the latter in more suitable condition to receive the preferential oilwetting treatment.
  • the method of treating a water-wet producing sand of an oil well to improve the production of oil relative to the production of water from the well which comprises flushing the well and the said water-wet producing sand with an aqueous alkaline solution substantially free from added dispersed solids and containing a clay-dispersing agent which disperses fine clayparticles from the pore space'of the sand grains to thereby flush out the pores /of the formation, and then distributing in the treated sand a chemical material which acts as a preferential oil-wetting agent to render the sand more permeable to oil and less permeable to water.
  • aqueous alkaline solution contains a calcium sequester-' ing agent having solvent action on calcium and magnesium salts.
  • aqueous alkaline solution contains a metaphosphate and a clay dispersing agent and base pH of about 5.
  • the aqueous alkaline solution contains a clay dispersing agent selected from the group consisting of the alkali metal salts of tannic, gallic, humic, pyrogallic, pyrophosphoric and silicic acids.
  • The. method of treating a water-wet producing sand of an oil well to improve the'production of oil relative to the production of water from the well which comprises flushing the well and the said water-wet producing sand with an aqueous alkaline solution substantially free from added dispersed solids and containing a strong clay deilocculating agent, and then coating the flushed sand with a preferentially oil-wettable material to render the sand more permeable to oil and less permeable to water.
  • the clay defiocculating agent is selected from the group consisting of the alkali metal salts of pyrophosphoric and silicic acids.
  • the step of pretreating the sand to receive the oil- ⁇ wettable coating which comprises flushing the sand with an aqueous-alkaline solution containing a hexametaphosphate.
  • the calcium sequestering agent is selected from the group consisting of the alkali metal salts of molecularly dehydrated phosphoric acids. and sulfur containing derivatives thereof and al- 2 kali metal salts of nitrogen-bearingcomplexes of i the moleoularly dehydrated phosphoric acids; which have solvent action on calcium and magnesium salts.
  • the method of treating a water-wet producing sand of an oil well to improve the production of oil relative to the production of water from the well which comprises treating the well and the said water-wet producing sand with an aqueous alkaline solution substantially free from added dispersed solids and containinga clay de-- flocculating agent and a wetting agent, and then coating the treated sand with a preferentially oilwettable material to render the sand more permeable to oil and less permeable to water.
  • the wetting agent is a synthetic organic detergent of the type of an alkali metal salt of a sulfated long chain aliphatic organic compound whose calcium salt is water soluble.

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Description

' easily wet by water than by oil.
1 Patented June24, 1941 um'rsb JSTA'TlE of Delaware No Drawing.
s PATENT oFFics ms'rimwr or on. WELLS Allen D. Gan-lion, Houston, Tex" assignor to The Tens Company, New
York, N. 2., a corporation Application October as, 1939, Serial No. 301,154
Claims. (01. 166-21 This invention relates to the treatment of an oil well, and more particularly to the chemical treatment of the sand adjacent a producing well in ,order to render the sand preferentially wet;
table by oil to thereby increase the proportion ofoil and decrease the proportion of water produced by that well.
This is a continuation-in-part of 'my copendilrgsapplication. Serial No. 212,972, filed June i0, It is recognized that ordinary sand is more It is further recognized that oil producing sands are predominantly water-wet. When the pore spaces oi an oil producing sand contain both water and oil the fact that the sand surfaces are water-wet will cause the .water to occupy the smaller capil-.
laries and crevices to theexclusion of the oil, thereby limiting the flow of the oil to the larger capillaries only, this flow of oil' through these capillaries being retarded because the pore spaces of the capillaries are substantially reduced in cross section by the presence of the relatively im-v mobile water film on the sand grains. The oil iiow' into and through the smaller capillaries and crevices is opposed by the interfacial tension .be-
tween the oil and the water. My invention resides in a method of causing oil to flow through all of the capillaries and crevices of an oil producing sand by removing the water film from the walls 01 the capillaries and crevices and rendering the surfaces oil-wettable. In this manner the flow of water into the well is retarded by the same force which obstructs thev flow of oil through the average water-wet oil producing sandl In Patent No. 2,024,119 issued to William V. Vletti and Allen D.Garrison, there is disclosed and claimed a method of treating a producing, sand of this character which is wet with water, by the depositing of a water and oil insoluble precipitate on thesand grains, which precipitate is of such character that it does not all or block the pore space of the sand and is preferentially wettable by oil so that the sand becomes wet with oil,'wh ereby'the proportion of oil produced by the well is increased while the proportion of water so produced is decreased. The present invention constitutes 'an improvement over the method of said patent, and involves the pretreatment or the producing sand so that the pore space of the sand is enlarged or increased and the sand rendered in more suitable condition to receive the preferentially oil-wettable coating which is then'deposited upon the sand grains.
In accordance with the present invention, the producing sand is first flushed with an aqueous alkaline solution which is eflective to disperse fine, clay particles and silt from the interstices of the sand and which may also dissolve certain calcium and magnesium salts present in the formation, as well as remove oil irom the pore space. This flushing treatment is then followed by a treatment to coat the sand grains with a water and oil insoluble precipitate which is preferentially oil-wettable. I
A satisfactory aqueous flushin'g medium for carrying out the first step of this process is an aqueous alkaline solution of an alkali metal hex-ametaphosphate such as sodium hexametaphosphate, potassium hexametaphosphate, lith-' iumhexametaphosphate and ammonium hexametaphosphate. The chemical formula usually ascribed to the hexametaphosphates is exemplifled by-that of the sodium salt (NaPOa) a. latter is available commercially in a. form which upon solution in water gives an alkaline reactlon. The presence of the metaphosphate compound in the aqueous flushing medium prevents precipitation of calcium and magnesium compounds or salts which may be dissolved from the formation, by rendering these calciumand magnesium compounds immune to reaction by repressing ionization thereof. It is believed that the hexametaphosphate compound reacts with calcium and magnesium ions, forming complex compounds which are only slightly ionized and which remain in the aqueous alkaline solution. The aqueous flushing medium is thereby rendered capable of dissolving and holding in solution increased quantities of such salts, so that an effecmay be used in conjunction with the metaphosphate. Examples of the former are alkali metal salts such as sodium carbonate, sodium pyrophosphate and the like, or balanced mixtures of alkali metal hydroxides with alkali metal salts of such acids as boric, phosphoric, carbonic, oxalic,
silicic and similar weak acids. Sufiicient buffer salt or salt mixture is added to the aqueous fiushzone. Examples of suitable clay dispersing col-v loidal agents of this character are the water soluble alkali metal salts of such organic acids as tannic acid, gallic acid; humic acid, ogalllc acid and the like. A small proportion of such colloidal agent is satisfactory, for example a proportion of .01% to .5% on the basis of the aqueous flushing medium.
In place of the metaphosphates mentioned above, other suitable calcium sequestering agents may be employed. For example, various molecularly dehydrated phosphates, such as the triphosphates, tetraphosphates and higher condensed nuclei phosphates of this character, as well as the sulfur containing derivatives thereof, such as the trithiophosphates, tetrathiophosphates, etc., may be employed. In addition, the nitrogenbearing complexes of the molecularly dehydrated phosphoric acids which possess calcium-sequestering action can be used. Examples of such nitrogen-bearing complexes are imidophosphoric acids, diamidophosphoric acids, phosphirnic acids and the like: 5 I
These calcium sequestering agents are employed in aqueous solution, preferably in the presence of a suitable buifer salt or buffer salt .mixture of the character described above to maintain the aqueous fiushing medium in a slightly alkaline state, for example of a pH from 8.0 to 11.5. A suitable clay dispersing colloidal agent of the character of the water soluble alkali obstruction to the flow through the pore space of the producing sand is due to clogging precipitates of calcium and magnesium compounds, or
when the water content of the producing sand contains dissolved calcium and magnesium salts which would result in such clogging precipitates in the absence of a suitable calcium sequestering agent.
However, it is not necessary in all cases to emthe clogging is due primarily to clay, very satis-' factory results are secured by initial flushing with a water solution of an alkali metal pyro- .phosphate or alkali metal silicate or other suitable agent having strong deflocculating properties. Moreover, any of the above mentioned ploy a calcium sequestering agent, and good re- I aqueous alkaline solutions or solutions containing a clay deflocculating agent can be combined with any of the calcium sequestering compounds capable of solvent action on the alkaline earth salts. This preliminary flushing step preceding the depositing of the preferentially oil-wettable coating is of particular advantage in the case of old wells where the production rate has declined due to the cloning of the pores of the producing formation, as well as where the ratio of water to oil produced from the formation may have substantially increased.
In accordance with the process of the present invention, a suitable aqueous alkaline solution of the character set out above is first forced into the well and into the sand adjacent the well to clean the pore space of the sand by removing the fine silt and clay and dissolving the soluble salts. This treatment is also efiective to flush out oil from the pore space, so that the sand grains will be left in freely exposed and suitable condition for the subsequenttreatment of depositing the preferentially oil-wettable precipitate thereon. This first treatment may be followed directly with solutions producing the desired oil-wettable precipitate, or an intermediate slug of water can be forced into the well between the first flushing treatment and the subsequent coating of the sands with the desired precipitate, or the fiushing liquid can be first removed from the sand and the well bore by pumping or bailing.
Following this initial treatment, the prepared sand bed is then treated to coat the sand grains with a thin adhering film of a water and oil in-. soluble precipitate which is preferentially wettable by oil. This may be accomplished in the manner disclosed in the above mentioned Patent No. 2,024,119. As set forth therein, there is forced into the well and into the sand adjacent the well a solution of a precipitatable compound of the preferential wetting character described. This is followed by a solution of a compound which is active to react with the first mentioned compound to produce the desired precipitate when these two solutions are brought into contact with each other within the producing sand being treated, whereby the precipitate so produced is effectively distributed and deposited throughout the treated sand zone. The procedure described above may be repeated one or more times, so as to secure the desired effective deposit and coating of the sand grains throughout the water-wet sand. Preferably, this is then followed by forcing a charge of oil into the well in order to force the chemicals farther out into the sands to increase the zone of treatment and to immediately create a zone of sand around the well which is wet by oil.
Suitable materials which possess the preferential wetting property include various water and oil insoluble salts of sulfonated oils, fats orfatty acids. For example, the alkaline earth and heavy metal salts, including those of calcium, barium, iron, manganese, zinc, tin, lead, and the like of sulfonated oils, fats or fatty acids may be employed. Natural fats such as tallow, olein, stearine and the like, which have been sulfonated by treatment with sulfuric acid, are suitable. Likewise sulfonated fatty acids formed by sulfonating stearic, palmitic, oleic, and the like are included. A very satisfactory and comparatively cheap material, which is a by-product of the petroleum industry, is the' sulfonic sludge acid derived from the treatment of petroleum oil with sulfuric acid, and termed herein a petroleum oil sulfonate. These various materials may con- ,veniently be used in the form of their alkali metal salts, whereby a water solution of the soluble salt may first be forced into the bore of the well and into the sand immediately surrounding the well. Then a water solution of a water soluble salt of calcium. barium, or other alkaline earth or heavy metal, such as a chloride or nitrate, is forced into the well and into the sand to react with the first mentioned solution to produce a precipitate of the water and oil insoluble metal salt ofthe sulfonated oil, fat or fatty acid,
upon the sand grains.
These particular salts are highly dispersed when formed in dilute solutions, and have the characteristic of not flocculating or cohering with themselves so that they .do not block or cement the sand being treated; rather, they have strong adherence for the sand grains and deposit in the form of a thin permanently adhering film agent or about these grains without materially reducing the porosity of the sand. These films are preferentially wettable by,oil, as opposed to water, so that after the treating solutions are removed from the well bore, which may be accomplished by flushing with oil or pumping, the sand grains become wet with oil. The net result is that the oil in flowing through the pores and capillaries of the producing sand does not have to overcome the interfacial tension between oil and water, so that the rate of production of oil from the treated sand is increased. Moreover, the sand has been converted to a state in which it is water repellent, so that at the same thne the proportion of water produced by that well is substantially 'decreased.
As a specific example of the present invention, the following is mentioned, A dilute water solution of sodium hexametaphosphate buffered with sodium carbonate and also containing sodium tannate is forced into the well and the producing sand. This is followed by a water wash to remove the first flushing liquid, then a dilute water solution of the sodium salt of petroleum sulfonate is introduced into the sand, and this is followed by a wash with a dilute solution of calcium chloride. Another charge of the sodium salt of petroleum sulfonate is then forced into the well, followed by another charge of the calcium chloride solution. This may be repeated still a third time, or even more, depending upon the extent of sand to be treated. Finally a quantity of oil is pumped into the well which will force the chemicals farther out into the sand and will renderthe sand in the immediate vicinity of the well wet by oil. a g
' As a further example of the present invention, the following is mentioned as particularly suitable in the case of an old well where the formation is particularly low in calcium and magnesium salts but has become clogged with deposits of clay or silt. A dilute water solution of sodium pyrophosphate is first forced into the well and agitated in the hole for a period of time with a spudder. I 'I'hisis followed by bailing to remove the first flushing liquid together with the de iiocculated clay and loosened sand carried in suspension therein. The producing sand may then be dried to remove water from the pore space thereof, asby suitable chemical or other dehydrating treatment, although this step may be omitted and good results obtained in many cases. A coating of the preferentially oil-wet- 'table material is then applied to the producing sand and finally 'a quantity of oil pumped into able wetting agent or surface tension depressant.
which latterfunctions to enable the fluid to be forced into the sand with greater ease, and assists .in w ttlng the clay and sand more rapidly so that it 2km: loosened. Any suitable wetting su ace tension depressant which is water soluble and non-reactive with the fluid, and does not form clogging precipitates with constituents of the formation can be employed, such as various alcohols, ketones, sulfonated organic detergents, and the like. Highly effective for this purpose are the alkali metal salts of sulfated long chain fatty alcohols, such as sodium oleyl sulfate, the alkali metal salts oflong chain fatty acid-taurine condensation products, and other synthetic organic detergents of this general type whose calcium salts are water soluble.
By way of example, a well in Duval County,
Texas, in which the sand was clogged with clay,
was treated byintroducing an aqueous solution of sodium hexametaphosphate containing an organic detergent known in the trade as Nacc0n0l." The fluid was agitated in the hole for about an hour with a spudder, and then the loosened sand and the deflocculated clay and shale were bailed out of the well. The cleaning eifect was unusually elfective in that the sand caved in so fast that the bailer was diflicult to empty, and the shale and clay were well deflocculated. This treatment obviously enlarged the hole and exposed fresh fo'rmation walls which were then-in an excellent condition toreceive a preferentially oil-wettable coating.
While in the preferential oil-wetting treatment described herein, mention has been made of the use of the particular treatment set forth and claimed in Patent No. 2,024,119 mentioned above,
it is to be understood that any other suitable accordance with the present invention, which relates to a combination of such preferential oilwetting treatment with a preliminary flushing of the sand bed such as to render the latter in more suitable condition to receive the preferential oilwetting treatment.
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:
1. The method of treating a water-wet producing sand of an oil well to improve the production of oil relative to the production of water from the well, which comprises flushing the well and the said water-wet producing sand with an aqueous alkaline solution substantially free from added dispersed solids and containing a clay-dispersing agent which disperses fine clayparticles from the pore space'of the sand grains to thereby flush out the pores /of the formation, and then distributing in the treated sand a chemical material which acts as a preferential oil-wetting agent to render the sand more permeable to oil and less permeable to water.
placed back 2. The method of claim 1, in which the aqueous alkaline solution contains a calcium sequester-' ing agent having solvent action on calcium and magnesium salts.
3. The method of claim 1, in which the aqueous alkaline solution contains a metaphosphate.
4. The method of claim 1- in which the aqueous alkaline solution contains a metaphosphate and a clay dispersing agent and base pH of about 5. The method of claim 1 in which the aqueous alkaline solution contains a clay dispersing agent selected from the group consisting of the alkali metal salts of tannic, gallic, humic, pyrogallic, pyrophosphoric and silicic acids.
6. The. method of treating a water-wet producing sand of an oil well to improve the'production of oil relative to the production of water from the well, which comprises flushing the well and the said water-wet producing sand with an aqueous alkaline solution substantially free from added dispersed solids and containing a strong clay deilocculating agent, and then coating the flushed sand with a preferentially oil-wettable material to render the sand more permeable to oil and less permeable to water.
7. The method of claim 6, in which the clay defiocculating agent is selected from the group consisting of the alkali metal salts of pyrophosphoric and silicic acids.
vert a water-wet producing sand to one which is preferentially wettable by oil by coating the sand grains with an oil-wettable precipitate, the step of pretreating the sand to receive the oil-\wettable coating which comprises flushing the sand with an aqueous-alkaline solution containing a hexametaphosphate.
10. The method of treating a water-wet producing sand of an oil well to improve the production of oil relative to the production of water from the well, which comprises flushing the well and the said water-wetproducing sand with an aqueous alkaline solution substantially free from added dispersed solids and containinga clay-deflocculating agent and having a pH of about 8.0
to 11.5 to flush out the pores of the producing a sand, and then coating the treated producing sand with a chemical material which acts as a preferential oil-wetting agent to render the sand more permeable to oil and less permeable to .water.
11. The method of treating a water-wet pro-- ducing sand of an oil well to improve the production of oil relativeto the production of water from the well, which comprises flushing the well and the said water-wet producing sand with an aqueous solution ofa calcium sequestering agent having solvent action on calcium and magnesium salts. and then coating the flushed sand with a preferentially oil-wettable material to render the sand more permeable to oil and less permeable to water;
- 12. The method as defined in claim 11, in
a which the calcium sequestering agent is selected from the group consisting of the alkali metal salts of molecularly dehydrated phosphoric acids. and sulfur containing derivatives thereof and al- 2 kali metal salts of nitrogen-bearingcomplexes of i the moleoularly dehydrated phosphoric acids; which have solvent action on calcium and magnesium salts.
13. The method of treating a water-wet producing sand of an oil well to improve the production of oil relative to the production of water from the well, which comprises treating the well and the said water-wet producing sand with an aqueous alkaline solution substantially free from added dispersed solids and containinga clay de-- flocculating agent and a wetting agent, and then coating the treated sand with a preferentially oilwettable material to render the sand more permeable to oil and less permeable to water.
14. The method according to claim 13, in which the wetting agent is a synthetic organic detergent of the type of an alkali metal salt of a sulfated long chain aliphatic organic compound whose calcium salt is water soluble.
15. The method according to claim '13, in which the aqueous alkaline solution is agitated within the hole of the well, and the resulting loosened sand and deflocculated clay and shale are removed by bailing prior to application of the preferentially oil-wettable coating.
LLEN D. GARRISON.
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Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2748080A (en) * 1953-03-02 1956-05-29 Cities Service Res & Dev Co Secondary recovery of petroleum by water flooding
US2813583A (en) * 1954-12-06 1957-11-19 Phillips Petroleum Co Process for recovery of petroleum from sands and shale
US2867279A (en) * 1957-03-18 1959-01-06 Nat Aluminate Corp Process and compositions for treating geological formations
US2920041A (en) * 1957-07-31 1960-01-05 Jersey Prod Res Co Waterflooding method of secondary recovery
US3021279A (en) * 1959-07-31 1962-02-13 American Cyanamid Co Method for the secondary recovery of oil
US3021901A (en) * 1959-01-07 1962-02-20 Dow Chemical Co Treatment of fluid-producing formations
US3032500A (en) * 1959-12-31 1962-05-01 American Cyanamid Co Sequestration of metal ions
US3160205A (en) * 1963-02-26 1964-12-08 Phillips Petroleum Co Secondary recovery water flooding process
US3191676A (en) * 1962-11-14 1965-06-29 Pan American Petroleum Corp Use of phosphates in a waterflooding process
US3233669A (en) * 1960-12-16 1966-02-08 Exxon Production Research Co Heating an underground reservoir by radioactivity to recover viscous and tarry deposits therefrom
US3254718A (en) * 1963-05-15 1966-06-07 Socony Mobil Oil Co Inc Acidizing subterranean formations
US3270808A (en) * 1963-02-25 1966-09-06 Phillips Petroleum Co Method for increasing subterranean formation permeability
US3330347A (en) * 1964-10-30 1967-07-11 Exxon Production Research Co Method of oil recovery using surfactants formed in situ
US3480083A (en) * 1968-03-27 1969-11-25 Nalco Chemical Co Waterflood process using organic phosphate esters
US3584687A (en) * 1970-02-03 1971-06-15 Nalco Chemical Co Inhibition of deposits from water or brine in underground formations
US4259486A (en) * 1980-02-04 1981-03-31 American Cyanamid Company Method for the aminoalkylation of phenol

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2748080A (en) * 1953-03-02 1956-05-29 Cities Service Res & Dev Co Secondary recovery of petroleum by water flooding
US2813583A (en) * 1954-12-06 1957-11-19 Phillips Petroleum Co Process for recovery of petroleum from sands and shale
US2867279A (en) * 1957-03-18 1959-01-06 Nat Aluminate Corp Process and compositions for treating geological formations
US2920041A (en) * 1957-07-31 1960-01-05 Jersey Prod Res Co Waterflooding method of secondary recovery
US3021901A (en) * 1959-01-07 1962-02-20 Dow Chemical Co Treatment of fluid-producing formations
US3021279A (en) * 1959-07-31 1962-02-13 American Cyanamid Co Method for the secondary recovery of oil
US3032500A (en) * 1959-12-31 1962-05-01 American Cyanamid Co Sequestration of metal ions
US3233669A (en) * 1960-12-16 1966-02-08 Exxon Production Research Co Heating an underground reservoir by radioactivity to recover viscous and tarry deposits therefrom
US3191676A (en) * 1962-11-14 1965-06-29 Pan American Petroleum Corp Use of phosphates in a waterflooding process
US3270808A (en) * 1963-02-25 1966-09-06 Phillips Petroleum Co Method for increasing subterranean formation permeability
US3160205A (en) * 1963-02-26 1964-12-08 Phillips Petroleum Co Secondary recovery water flooding process
US3254718A (en) * 1963-05-15 1966-06-07 Socony Mobil Oil Co Inc Acidizing subterranean formations
US3330347A (en) * 1964-10-30 1967-07-11 Exxon Production Research Co Method of oil recovery using surfactants formed in situ
US3480083A (en) * 1968-03-27 1969-11-25 Nalco Chemical Co Waterflood process using organic phosphate esters
US3584687A (en) * 1970-02-03 1971-06-15 Nalco Chemical Co Inhibition of deposits from water or brine in underground formations
US4259486A (en) * 1980-02-04 1981-03-31 American Cyanamid Company Method for the aminoalkylation of phenol

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