|Publication number||US2262428 A|
|Publication date||Nov 11, 1941|
|Filing date||May 21, 1938|
|Priority date||May 11, 1935|
|Publication number||US 2262428 A, US 2262428A, US-A-2262428, US2262428 A, US2262428A|
|Inventors||Lietz Wilhelm Tempelaar|
|Original Assignee||Shell Dev|
|Export Citation||BiBTeX, EndNote, RefMan|
|Referenced by (30), Classifications (8)|
|External Links: USPTO, USPTO Assignment, Espacenet|
Patented Nov. ll, 1941 PROCESS FOR THE TREATMENT OF OIL OR GAS WELLS Wilhelm Tempelaar Lietz, The Hague, Netherlands, assignor to Shell Development Company, San Francisco, Calif., a corporation of Delaware No Drawing. Application May 21, 1938, Serial No. 209,364. In the Netherlands May 11, 1935 2 Claims. (01. 166-21) L 'part of my application Serial No. 77,550, filed May In many cases, the decrease in production of oil and gas wells is due not to actual exhaustion of the well reservoir, but to various other causes:
for example, a considerable portion of the original oil may remain adhering to the sands of the formation; the pores, crevices, and flow channels of the producing formation may become clogged due to the precipitation of mineral deposits from the formation water or the mud fluid; gummy resinous, asphaltic or other organic solid matter may accumulate on the walls of the borehole, or in the pores, crevices and flow channels of the adjoining formation, blocking or reducing the flow of oil or gas to the well; finally, connate water, or water forced into the formation during the drilling period, may tenaciously adhere to the sand particles and decrease the permeability of the formationto the flow of oil.
Various methods have been developed to remedy these conditions, such as acidizing methods, flooding methods, treatments with heat-generating mixtures, treatments with solvents such as benzol, etc.
All of these methods are, however, subject to inherent limitations, and can therefore be successfully used only to attain limited objectives. Thus, treatment with acids is not effective in formations devoid of calcareous matter; flooding requires a plurality of suitably located wells; washing solvents such as carbon disulphide, carbon tetrachloride, benzol or gasoline are ineffective in cases where the low permeability of the forma-: tion is due, for example, to the presence therein of connate waters, etc.
The object of the present invention is to pro vide a process for treating oil wells passing through non-calcareous formations whose permeability is decreased by the presence therein of water and of asphaltic or gummy deposits, and, more specifically, to provide a method whereby the well and the adjacent formations are treated with a solvent capable at once to dissolve said organic deposits and the water held in the small capillary spaces of the sand.
Briefly stated, the present process consists in introducing into a well, preferably under pressure, a washing liquid which does not chemically attack the rock, causing it to penetrate into the formation, dissolving therein the gummy and resinous deposits and the water held between the sand grains by virtue of its surface tension, and withdrawing, after a desired time, the washing liquid from the same well together with the dissolved organic deposits and connate waters, for example, by releasing the pressure.
The washing liquid may be introduced into the oil formation in various ways. The desired amount of liquid, that is, an amount sufficient to impregnate the oil-bearing formation over its entire depth and to a desired radius around the well, may be run into the well through the tubing with the casing head open during this process. Another liquid, which may be immiscible with the washing liquid, such as water, oil, etc. may then be pumped into the casing and tubing simulta-- neously to force the washing liquid into the formation. Likewise, air or gas pressure may be applied in the same way' and for the same purpose to the washing liquid charge. After the washing liquid has penetrated into the formation and remained therein for a desired period of time, the pressure on the well may be released, the formation pressure forcing the washing liquid, together with the dissolved water and gummy or resinous materials, back into the well, from which it may be withdrawn by pumping or swabbing;
It has been found that the following substances are particularly suitable for the purposes of this invention: heterocyclic nitrogen base compounds of the type of pyridine or quinoline, their homologues and derivatives, such as picolines, lutidines, alp'ha-collidines, pyridine-carboxylic acids, pyridine-sulphonic acids, hydroxy-pyridines, aminoand di-amino-pyridines, piperidine, quinolinecarboxylic acids, hydroxy-quinoline, and, in general, nitrogen bases obtained from coal tar and cracked petroleum products by various processes such, for example, as extraction with mineral acids. purposes of this invention in such form as they are obtained in commercial processes, that is, in the form of mixtures containing various impurities, or they may be subjected to a preliminary purification to increase the percentage of the effective compounds contained therein.
These compounds may further be used either in pure form, or in any mixture with each other, or in admixture with suitable solvents, such as ketones, for example, methyl ethyl ketone, methyl propyl ketone, diethyl ketone; alcohols, for example, methyl alcohol, isopropyl alcohol, secondary butyl alcohol; ethers, for example, dioxane, tetra methylene oxide, furan; ether alcohols, for example, ethyl ether of ethylene glycol and diethylene glycol-monethylether; esters, for example, butyl lactate, glycol diacetate, carbitol or cellosolve acetates; acetone tops; benzol, gasoline, etc. The solvent is selected'in each case-depending on the particular nitrogen base compound used. Thus, for example, pyridine which is miscible in any proportions with water, can be used either alone, or with any of the above 'sol- The nitrogen bases may be used for the vents, including the water-immiscible solvents such as benzol or gasoline, since it is in itself effective in dissolving the water within the formation. Other agents, such as quinoline, which have only a limited solubility in water, but are miscible in all proportions with alcohol and ether, should preferably be used in combination with the latter as solvent, and will operate to dissolve the asphaltic deposits, while the alcohol or ether solvent will dissolve and act to remove the connate water.
Especially good results are obtained, by using the treating agents and compositions shown in Table I.
Table I Treating Agent 4 Percent Percent 1 Pyridine 100 2 Nitrogen bases (fraction boiling 160230 C.).
3 Nitrogen bases Acetone Acetone Methyl propyl ketone.
Acetone tops In general, water-soluble agents, such as pyridine, maybe used in any concentration, preferably between 10040% limits. Agents which are only partially water-soluble, such as quinoline or.
the commercial nitrogen bases, can be used preferably in 60-40% concentrations.
The treating agents listed above possess the following properties which are essential for the purposes of this invention:
(1) They quickly and completely dissolve the organic deposits plugging a formation. Pyridine, its derivatives, and nitrogen bases, in general,
-' have a preferential solvent power for asphalt and are therefore especially effective against organic deposits of a gummy or asphaltic nature.
(2) They are capable of releasing the connate water held in the capillary spaces of the sand by lowering its surface tension and also the interfacial tensionbetween the water and the oil. For example, the addition of 20% by volume ofpyridine reduces the surface tension of water by- 51%,and its interfacial tension with oil by 89%. These agents are further capableof dissolving or absorbing the released connate water, whereby the latter may subsequently be removed from the formation together with the treating agent.
(3) They have further a favorable effect on oil sand, and particularly on silicious sand, in that they do not increase its wetting properties for water. The connate water removed from-said sand is not therefore immediately replaced by 'edgewater flowing through the formation, and
the permeability of said sand to oil flow is increased.
These agents are therefore considerably more. effective in treating formations whose permeabilwhich are capable of lowering the surface tension of water, but are poor solvents for asphaltlc deposits, are relatively ineffective for the purposes of this invention. These solutions tend, moreover,
' to form emulsions whereby the permeability of Table II Perme- Permeability abilityv Increase Core before after in perme- No Treating agent trcattreatability ment ment in per- (in milli- (in millicent darcys) darcys) 1 Carbon disulphide 3.05 4. 8 57 Ijyridine 3. 05 5. 4 77 2 Carbon tetrachloriricuu'u 1.96 2. 47 26 Methyl alcohol 1.96 3. 10 58 Pyridine 1, 96 4. 118
3 1% solution of alkyl sulfates (Cm( l 1.73 1.56 9.8 Nitrogen bases (boiling rnmze l50-2l5 (3,) 1.73 2. 08 +20 Pyridine 1. 73 2. 15 +24 1 Decrease.
plete removal from the ground of the treating agent used first, before applying the second treatment, since a reaction within the formation between, for example, hydrochloric acid and the nitrogen bases of the present reaction may cause a precipitation of undesirable salts and lead to a serious plugging of the formation.
I claim as'my invention:
1. In the process of treating wells passing through formations obstructed by the presence therein of organic deposits and water, the steps of introducing into the well an acid free treating liquid comprising pyridine, forcing said liquid into the formation, allowing said liquid to dissolve said organic deposits and water, and withdrawing the treating liquid together with the dissolved matter from the well.
2. In the process of treating wells passing through formations obstructed by the presence therein of organic deposits and water, the steps of introducing into the well an acid-free treating liquid comprising a fraction of heterocyclic nitrogen base compounds obtained in cracking coaltar and petroleum products, said fraction having a boiling range from to 230 C., forcing said liquid into the formation, allowing said liquid to dissolve said organic deposits and said water, and withdrawing the treating liquid together with the dissolved matter from the Well.
WILHELM TEIVHPELAAR LIETZ.
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US2419755 *||May 26, 1943||Apr 29, 1947||Union Oil Co||Chemical treatment of oil sands|
|US2465237 *||Mar 31, 1937||Mar 22, 1949||Delmar H Larsen||Treatment of oil wells|
|US2761835 *||Nov 18, 1954||Sep 4, 1956||Gulf Research Development Co||Treatment of clays|
|US2761836 *||Nov 18, 1954||Sep 4, 1956||Gulf Research Development Co||Treatment of clays|
|US2761837 *||Nov 18, 1954||Sep 4, 1956||Gulf Research Development Co||Treatment of clays|
|US2761838 *||Nov 18, 1954||Sep 4, 1956||Gulf Research Development Co||Treatment of clays|
|US2761839 *||Nov 18, 1954||Sep 4, 1956||Gulf Research Development Co||Treatment of clays|
|US2761840 *||Nov 18, 1954||Sep 4, 1956||Gulf Research Development Co||Treatment of clays|
|US2761841 *||Nov 18, 1954||Sep 4, 1956||Gulf Research Development Co||Treatment of clays|
|US2761842 *||Nov 18, 1954||Sep 4, 1956||Gulf Research Development Co||Treatment of clays|
|US2761843 *||Nov 18, 1954||Sep 4, 1956||Gulf Research Development Co||Treatment of clays|
|US3016351 *||Oct 30, 1959||Jan 9, 1962||Gen Aniline & Film Corp||Process for improving secondary oil recovery|
|US3016352 *||Oct 30, 1959||Jan 9, 1962||Gen Aniline & Film Corp||Process for improving injectivity in secondary oil recovery|
|US3064732 *||Nov 16, 1959||Nov 20, 1962||Pure Oil Co||Method for increasing formation permeability|
|US3079336 *||Mar 22, 1960||Feb 26, 1963||Jersey Prod Res Co||Alcohols in conjunction with water thickeners for a secondary recovery process|
|US3131759 *||Jun 19, 1959||May 5, 1964||Socony Mobil Oil Co Inc||Method of treating oil-productive subterranean formations|
|US3179675 *||Jun 18, 1963||Apr 20, 1965||Warner Lambert Pharmaceutical||Purification and stabilization of quingestrone|
|US3395757 *||Jan 16, 1964||Aug 6, 1968||Electro Chem Corp||Method and composition for removing and inhibiting paraffin deposition|
|US3446620 *||Mar 18, 1965||May 27, 1969||Addressograph Multigraph||Process for developing diazotype materials|
|US3941192 *||Aug 26, 1974||Mar 2, 1976||Texaco Inc.||Method for recovering high asphaltene content petroleum using surfactants|
|US5779938 *||Aug 24, 1995||Jul 14, 1998||Champion Technologies, Inc.||Compositions and methods for inhibiting corrosion|
|US7122146||Apr 18, 2005||Oct 17, 2006||Akopyan Razmik L||Injection molding of polymers by microwave heating|
|US8871694 *||Jul 8, 2010||Oct 28, 2014||Sarkis R. Kakadjian||Use of zeta potential modifiers to decrease the residual oil saturation|
|US9334716 *||Mar 15, 2013||May 10, 2016||Halliburton Energy Services, Inc.||Treatment fluids comprising a hydroxypyridinecarboxylic acid and methods for use thereof|
|US20040222554 *||Jun 15, 2004||Nov 11, 2004||Akopyan Razmik L.||Microwave molding of polymers|
|US20050184434 *||Apr 18, 2005||Aug 25, 2005||Razmik Akopyan||Injection molding of polymers by microwave heating|
|US20110005756 *||Jul 8, 2010||Jan 13, 2011||Clearwater International, Llc||Use of zeta potential modifiers to decrease the residual oil saturation|
|US20130269941 *||Mar 15, 2013||Oct 17, 2013||Halliburton Energy Services, Inc.||Treatment Fluids Comprising a Hydroxypyridinecarboxylic Acid and Methods for Use Thereof|
|DE2846977A1 *||Oct 28, 1978||May 10, 1979||Exxon Research Engineering Co||Salzwasservertraegliche korrosionsinhibitoren|
|WO1997008264A1 *||Aug 22, 1996||Mar 6, 1997||Champion Technologies, Inc.||Compositions and methods for inhibiting corrosion|
|U.S. Classification||507/242, 507/935, 507/936|
|Cooperative Classification||C09K8/524, Y10S507/936, Y10S507/935|