US2139595A - Method for dissolving paraffing and wax - Google Patents

Method for dissolving paraffing and wax Download PDF

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Publication number
US2139595A
US2139595A US49316A US4931635A US2139595A US 2139595 A US2139595 A US 2139595A US 49316 A US49316 A US 49316A US 4931635 A US4931635 A US 4931635A US 2139595 A US2139595 A US 2139595A
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solvent
wax
pipe
tubing
well
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US49316A
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Lerch William Bruce
Ted M White
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Phillips Petroleum Co
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Phillips Petroleum Co
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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
    • C09K8/52Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning
    • C09K8/524Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning organic depositions, e.g. paraffins or asphaltenes
    • 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
    • Y10S507/927Well cleaning fluid
    • Y10S507/929Cleaning organic contaminant
    • Y10S507/931Organic contaminant is paraffinic

Description

Dec. 6, 1938. w. B. LERCH Er AL 2,139,595
METHOD FOR DISSOLVING PARAFFIN AND WAX Filed Nov. 11, 1935 WILLIAM BRUCE LERCH TED M. WHITE BY M4/CCW ATTORNEYS.
Patented Dec. 6,
E i GFICE METHOD FOR DISSgIgiING PARAFFIN AND William Bruce Lerch and Ted M. White, Bartlesville, Okla., assignors to Phillips Petroleum Company, Bartlesville, Okla., a corporation 'of Delaware Application November 11, 1935, Serial No. 49,316
l Claim.
This invention relates to the removal of parafn and wax from oil wells, pipe lines, and the like, and in particular it relates to and has for its objects the dissolving, cutting and removing of wax or paraiiin from the casing and tubing pipes of oil wells and other portions thereof, and from pipe lines and other places where it may occur.
Further objects of this invention are to provide a parain and wax solvent and a method of applying the same for removing parailin and wax deposits from wells and the pipes therein which is readily soluble in and miscible with the oil and/or water occurring in the well.
In the production of crude oil by various methods such as from naturally owing wells, wells articially owed, and wells equipped with various pumping devices there is formed in the reservoir area at the bottom of the well hole where the oil accumulates, in the tubing and in the annular space between the tubing and the casing pipe, material deposits of paramn and/or amorphous wax. The accumulation of this paraffin or Wax in the wells occurs to such an extent that it completely clogs the interstices of the producing strata, and otherwise attaches itself to the tubing and casing pipe so that in extreme cases it is impossible to produce oil from the well.
The drawing diagrammatically illustrates in cross-section an oil well showing at the bottom thereof the reservoir l0, and the casing pipe Il, and a string of tubing i2. For the purpose of describing the present invention it will be noted that the casing pipe Il is provided with a cap i3 at l the top portion thereof into which there is inserted a pipe l, while the string of tubing l2 is also provided with a cap l at the top thereof and connected thereto is a pipe i6.
This invention relates both to the product for dissolving and cutting the paran and wax from the well hole and to a method of applying and utilizing the solvent in so removing the paraffin and wax.
We propose to inject into the well hole,- either through the tubing or the casing pipe, sufhcient amounts of paraiiln and wax solvents in the form of liquid hydrocarbons of the paraffin or methane series. These hydrocarbons will be saturated or unsaturated and preferably distillates of that series, and as such will preferably consist of such hydrocarbon liquids as kerosene, naphtha, casinghead or natural gasoline, gasoline of motor fuel specifications, and kettlebottoms, which may be described as a residue distillate obtained in the manufacture of natural (Cl. 16S-21) gasoline or any suitable unsaturated petroleum hydrocarbon distillate.
When the above described solvents are used in wells of relatively shallow depth, for instance up to 3,000 feet, it has been found that from ten to one hundred (100) gallons of any of the above mentioned solvents will be sumcient to dissolve and cut the wax and paraflln in the well. However, if the wells to be treated are of considerable depth, for instance over 3,000 feet, lt ls best to use larger amounts ranging from one thousand (1,000) to three thousand (3,000? (55,? of solvent. These figures relative tc the quantity of solvent to be used are based upon the average wells classied as deep and shallow and are not intended to be the exact amounts for any one well.
With further consideration of the drawing, assume that the wax and paraiiin nave materially clogged the casing, or tubing pipes, and the reservoir area, and are clinging to the surface thereof in large quantities at the points designated by the reference letter W. In such a case any of the parafn or wax solvents as above described, for instance, kerosene or gasoline could be injected through the pipe lli into the annular space between the casing pipe il and the tubing l2, and by applying pressure thereto, and/or by the utilization of a pump, the solvent could be pumped or forced to the bottom of the well i0 and up into the tubing l2 and back to the surface by way of pipe i6. If a pump is used to circulate the solvent in the manner described, it would be continuously returning to pipe i4 as it issues from pipe I6, and causing the solvent to recirculate in the manner described. Although it should be understood that in lieu of introducing the solvent at It and allowing it to escape from the well at I6, it could just as Well be introduced into the pipe I6 connected with the tubing I 2 and allowed to issue from the Well by way of pipe It connected to the casing pipey Il. In either event, after several cycles of the circulation as above described, the pump, or any other motive force used, would be discontinued for an appreciable period of time, allowing the solvent to remain stationary in the well hole and in the casing and tubing pipe, allowing it to have a soaking action to cut and dissolve the Wax and paraiiin formed on the surfaces thereof. After such soaking or standing period, the pump or other motive force would again put the admixture of solvent and oil of the well into motion and` circulate it as previously described. The method above described of circulating the solvent in the Well can also be conducted without the intermittent soaking or standing phase. It should therefore be appreciated that it may not be necessary in all cases to allow the solvent to stand stationary as described, but in wells which are clogged to only a minor degree with the wax and paramn, it may only be necessary to circulate the solvent therein for a short period of time to sumciently'dissolve and cut the same. It is therefore proposed to allow the solvent to remain stationary in the well between cycles of circulating the same only when' the well is clogged with paraffin and wax to a major degree in order that the solvent may .have a longer period of time to dissolve the wax and so more eectively remove the same.
In lieu of causing the solvent to circulate in and out of the well as above described, it has been found that if the wax is present on the interior walls of the casing pipe and on the exterior walls v of the tubing pipe, then the solvent may be introduced into the space between the casing and tubing pipes by way of pipe I 4 and thereafter gas under pressure may be introduced to the interior of the tubing pipe by way of pipe I6, and by alternately applying high and low pressure to the gas so introduced, the admixture of oil and solvent present in the .well in the form of a liquid column between the casing and tubing pipes will be caused to reciprocate up and down, and such a rocking motion will serve to Wash the walls of these pipes and cut therefrom the wax and paraf- Here again it has been found advantageous to discontinue this reciprocating or rocking motion of the solvent at various intervals and to allow it to remain stationary'so that the solvent may have the opportunity of soaking into and cutting the wax, after which the reciprocating movement oi' the column oi' solvent is again resorted to in order that the paraffin and wax may be removed. After treating the walls of the pipes in this manner the solvent is then removed by applying continuous pressure to the tubing, which will thereby force the solvent up into the top portion of the annular space formed by the pipes vI2l and II and .cause it to ultimately ow through pipe I4, by which it is removed.
Here again it is to be understood that in lieu of introducing the solvent by way of pipe I4 into the annular space between the casing pipe and the tubing, the solvent may be introduced into pipe I6 and thence into the tubing I2. This latter mode of application is resorted to particularly when it is the interior walls of the tubing that contain the accumulation of wax or paraln. In this last mode of application the gas under pressure would then be introduced into the pipe I 4 and thence into the annular space between the tubing and casing, and by the alternate application of high and low pressures as above described, the liquid column of solvent and oil in the tubing pipe I2 will be caused to reciprocate up and down, and so in addition to acting as a solvent for cutting paraflin and wax from the interior of tubing, it will also wash the tubing walls and thereby assist in cleansing them of deposits. As'previously mentioned in connection with the introduction of the gas through pipe IB and into the tubing I2, and the introduction of the liquid column of solvent through pipe I4 and into pipe II, the gas being introduced into pipe I4 in this present case, may also be so controlled as to allow the column of solvent in the tubingpipe I2 to remain at a standstill in order that it may soak the parain and wax adhering thereto in order to cut the same from the walls, and after such soaking action the pressure may again be applied through pipe I4 in alternate high and low amounts to cause the column of solvent in the tubing pipe to reciprocate up and down and so wash the walls clean. The solvent in the tubing pipe I2 will, of course, be removed by applying suilicient pressure through pipe I4 so as to force the solvent up through ,the tubing pipe and out through pipe I6. By utilizing the solvents above referred to, and the method of applying them as just described, it has been found that a Well which is but moderately clogged with parailin or wax may be treated in the above manner for a period of from two to three hours', and it will thereafter be found that the solvent has removed substantially allparailln and wax formerly adhered to the walls of the pipes and the well hole wall surfaces, leaving the same free and clean for production. However, when the well contains material amounts of paraffin and wax, it has been found necessary in such cases to treat the Well for a greater period of time, usually in the neighborhood of from five to ten hours.
In some wells the wax and paraflin deposits are present in such large amounts that the solvents previously described will remove them only after a prolonged application, and when such wells are being treated as previously described, it has been found necessary to incorporate in such solvents some substance which is a particularly active wax or parain solvent and which will materially aid in the cutting and dissolving of paraffin. A predominant amount of kettlebottoms and/or naphtha when used with a relatively small proportion of naphthalene akes or carbon tetrachloride, Will produce a highly satisfactory solvent for cutting parain and Wax from wells. In the above solvent, the flaked naphthalene or carbon tetrachloride, whichever is used, will form the minor portion of the solvent and should not be over substantially ten percent (10%) by weight, nor materially less than three percent (3%) by weight, the remaining portion of the solvent being composed of -such substances as kettlebottoms or naphtha. This solvent will, of course, be used in the exact manner as previously described.
When the wax or paraffin occurs in wells which are producing a material amount of water, which may be brine, it has been found convenient and more eicient to add to the solvent some material which will render the same water soluble in order that it will be miscible with the water, and in particular with that occurring in the bottom portion of the well hole adjacent the reservoir area, which is shown in the drawing at I0, to render the solvent miscible therewith. Any suitable Water soluble agent may be added, such as any of the modified fatty acids, particular reference being had to soaps or any other type of saponifying agent. In this latter type of solvent, it is to be understood that any of-the solvents heretofore described could be used, and that the same may readily be rendered water soluble. However, for a particular example of a wax solvent for use in wells which are producing material amounts of water, it is proposed to use such a substance as kettlebottoms or naphtha, and to constitute approximately 97% by weight of the solvent, and naphthalene flakes or carbon tetrachloride and the like to be present and constitute approximately 3% of the wax solvent. To such a solvent mixture there would then be added suiicient quantities of a saponifying agent such as soap to render the solvent miscible with water. It is to 7l be further understood that this last described water soluble solvent would be used in substantially the same manner as the solvents heretofore described.
After the well has been treated in any of the above described manners, the well may then be put on production and the oil produced will contain the solvent admixed therewith which during the course of rening the oil will result in the recovery of the solvent as one of the products. Therefore it can readily be appreciated that the improved method and product for cutting and dissolving parafin and wax deposits in wells and removing them is extremely economical.
While we have described and explained our invention with particular reference to oil wells, it is to be understood that we do not limit our invention to such a specic use, as the same canbe used with equal eiiciency in wells of any type, and also in the cleansing and removing of parailin and wax from pipe lines and similar conduits by merely applying the principle taught in our specification.
What we claim and desire to secure by Letters Patent is:
The method of cleaning wells and well pipes of deposits of paraffin and Wax which consists in introducing into a well hole a water miscible liquid wax solvent in the form of a column of liquid hydrocarbons containing a minor portion of modied fatty acid saponifying agentand ake naphthalene and causing said column of solvent to be reciprocated up and down in the well to dissolve the paraffin therein.
W. BRUCE'LERCH. 'IED M. WHITE.
US49316A 1935-11-11 1935-11-11 Method for dissolving paraffing and wax Expired - Lifetime US2139595A (en)

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Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2711392A (en) * 1952-02-06 1955-06-21 August W Willert Jr Method for recovering the oil from oil wells
US2734861A (en) * 1956-02-14 Composition and process for plugging
US2765850A (en) * 1953-05-22 1956-10-09 Texas Co Production of formation-clogging liquid hydrocarbons
US2879847A (en) * 1954-11-29 1959-03-31 August W Willert Jr Process for increasing the flow in oil wells
US2998066A (en) * 1957-04-19 1961-08-29 Charles N Mcclendon Method of treating wells
US3051653A (en) * 1959-10-06 1962-08-28 Halliburton Co Paraffin control composition and method
US3076506A (en) * 1959-07-10 1963-02-05 Phillips Petroleum Co Enlargement of boreholes in carbonaceous strata for in situ combustion
US3160206A (en) * 1961-06-07 1964-12-08 Shell Oil Co Method of cleaning permeable formations
US3172473A (en) * 1962-06-28 1965-03-09 Crowley Tar Products Company I Method of improving well flow
US3279541A (en) * 1965-08-20 1966-10-18 Halliburton Co Method for removing paraffinic and asphaltic residues from wells
US3344859A (en) * 1964-04-30 1967-10-03 Sinclair Research Inc Method of inhibiting paraffin deposition in oil wells
US3424249A (en) * 1966-10-19 1969-01-28 Shell Oil Co Cleaning steam injection well tubing string in situ
US3442136A (en) * 1966-08-10 1969-05-06 Itt Automatic fluid sampler
US3566970A (en) * 1969-02-13 1971-03-02 Dresser Ind Method of injecting treating liquids into well tubing
US4646837A (en) * 1985-09-24 1987-03-03 Shell Oil Company Process for removal of wax deposits
US20110146999A1 (en) * 2009-12-16 2011-06-23 Flo-Solutions Ltd. Method and Apparatus for Dewatering Using Methane
US10711176B2 (en) * 2018-10-03 2020-07-14 David O. Trahan Method, process, apparatus and chemicals to produce and inject paraffin treating compounds

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2734861A (en) * 1956-02-14 Composition and process for plugging
US2711392A (en) * 1952-02-06 1955-06-21 August W Willert Jr Method for recovering the oil from oil wells
US2765850A (en) * 1953-05-22 1956-10-09 Texas Co Production of formation-clogging liquid hydrocarbons
US2879847A (en) * 1954-11-29 1959-03-31 August W Willert Jr Process for increasing the flow in oil wells
US2998066A (en) * 1957-04-19 1961-08-29 Charles N Mcclendon Method of treating wells
US3076506A (en) * 1959-07-10 1963-02-05 Phillips Petroleum Co Enlargement of boreholes in carbonaceous strata for in situ combustion
US3051653A (en) * 1959-10-06 1962-08-28 Halliburton Co Paraffin control composition and method
US3160206A (en) * 1961-06-07 1964-12-08 Shell Oil Co Method of cleaning permeable formations
US3172473A (en) * 1962-06-28 1965-03-09 Crowley Tar Products Company I Method of improving well flow
US3344859A (en) * 1964-04-30 1967-10-03 Sinclair Research Inc Method of inhibiting paraffin deposition in oil wells
US3279541A (en) * 1965-08-20 1966-10-18 Halliburton Co Method for removing paraffinic and asphaltic residues from wells
US3442136A (en) * 1966-08-10 1969-05-06 Itt Automatic fluid sampler
US3424249A (en) * 1966-10-19 1969-01-28 Shell Oil Co Cleaning steam injection well tubing string in situ
US3566970A (en) * 1969-02-13 1971-03-02 Dresser Ind Method of injecting treating liquids into well tubing
US4646837A (en) * 1985-09-24 1987-03-03 Shell Oil Company Process for removal of wax deposits
US20110146999A1 (en) * 2009-12-16 2011-06-23 Flo-Solutions Ltd. Method and Apparatus for Dewatering Using Methane
US10711176B2 (en) * 2018-10-03 2020-07-14 David O. Trahan Method, process, apparatus and chemicals to produce and inject paraffin treating compounds

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