US3796265A - Method for producing high hydrogen sulfide content gas wells - Google Patents
Method for producing high hydrogen sulfide content gas wells Download PDFInfo
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- US3796265A US3796265A US00260682A US3796265DA US3796265A US 3796265 A US3796265 A US 3796265A US 00260682 A US00260682 A US 00260682A US 3796265D A US3796265D A US 3796265DA US 3796265 A US3796265 A US 3796265A
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- tubing string
- fluid
- sulfur
- production tubing
- string
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 83
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 title claims abstract description 12
- 229910000037 hydrogen sulfide Inorganic materials 0.000 title claims abstract description 12
- 239000007789 gas Substances 0.000 title abstract description 6
- 239000012530 fluid Substances 0.000 claims abstract description 123
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims abstract description 60
- 229910052717 sulfur Inorganic materials 0.000 claims abstract description 55
- 239000011593 sulfur Substances 0.000 claims abstract description 55
- 230000008021 deposition Effects 0.000 claims abstract description 12
- 238000001556 precipitation Methods 0.000 claims abstract description 5
- 230000015572 biosynthetic process Effects 0.000 claims description 41
- 238000002347 injection Methods 0.000 claims description 25
- 239000007924 injection Substances 0.000 claims description 25
- 238000000034 method Methods 0.000 claims description 25
- 239000002904 solvent Substances 0.000 claims description 17
- 238000004891 communication Methods 0.000 claims description 15
- 238000010438 heat treatment Methods 0.000 claims description 7
- 238000002844 melting Methods 0.000 claims description 7
- 230000008018 melting Effects 0.000 claims description 7
- 239000002244 precipitate Substances 0.000 claims description 5
- 239000010779 crude oil Substances 0.000 claims description 4
- 239000011810 insulating material Substances 0.000 claims description 3
- 238000012856 packing Methods 0.000 claims description 2
- 238000005755 formation reaction Methods 0.000 description 32
- 239000003921 oil Substances 0.000 description 19
- 238000000151 deposition Methods 0.000 description 10
- 230000007423 decrease Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 239000004568 cement Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 239000008186 active pharmaceutical agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000012937 correction Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000004299 sodium benzoate Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 150000003463 sulfur Chemical class 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
Images
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B36/00—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
-
- 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
- C09K8/52—Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning
- C09K8/528—Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning inorganic depositions, e.g. sulfates or carbonates
- C09K8/532—Sulfur
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B36/00—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
- E21B36/003—Insulating arrangements
Definitions
- This prior art production technique has the disadvantage that injected fluid, which is generally more dense than produced fluid, is required in such quantity as to significantly increase the pressure gradient in the tubing string. This imposes an increased back-pressure on the productive formation and results in decreased well deliverability.
- the large amount of elemental sulfur contained in the injected fluid must be separated from that fluid at the surfaceif the sulfur is to be recovered or if the solvent is to be reused. This may require a substantial amount of separating equipment and attendant expense.
- sulfur-containing fluid' can be produced from a subsurface formation without plugging of the production tubing from sulfur deposition by flowing the fluid to the surface through a production tubing string while heating the flowing sulfurcontaining fluid indirectly by heating the production tubing string and thereby conductively heating the flowing fluid.
- heat may be supplied to the production tubing string from electric heating coils disposed around the tubing string or by circulating a hot fluid into the well and into contact with the exterior of the production tubing string.
- the flowing sulfurcontaining fluid may be concurrently heated directly by injecting a hot sulfur-solvent into the well and into contact with the produced sulfur-containing fluid.
- a well bore extending from the surface to a formation of interest containing a fluid having a high hydrogen sulfide content is at least partially lined with a large diameter tubular casing and is completed so as to be in fluid communication with the formation.
- a first string of tubing, a production tubing string is then extended into the well to a point adjacent the bottom of the productive formation.
- the casing-production tubing string annulus is packed off with a pack-off means set above the productive formation and a second string of tubing, a hot-oil injection string, is extended into the well bore and through the pack-off means to connect this hot oil injection string in fluidcommunication with the packed-off interval of the well bore opposite the productive formation.
- a third string of tubing, an insulated circulating string is then installed in the casingproduction tubing annulus so as to extend throughout a major length of the annulus above the pack-off means.
- Hydrogen sulfide rich fluid may. than be produced from the productive formation through the production tubing string.
- a hot fluid such as steam having a temperature about 300 F, is circulated down the insulated circulating tubing string and up the casing-production tubing annulus in an amount sufficient to heat the produced fluid in the production tubing string and thereby maintain the temperature of this fluid above a pre-detennined minimum temperature, which is preferably above the melting point of sulfur.
- a fluid in which sulfur is soluble such as a light substantially sulfur-free crude oil
- a fluid in which sulfur is soluble advantageously can be injected down the injection tubing string into the packed-off interval of the well bore and produced up the production tubing string with the reservoir fluid in an amount sufficient to dissolve precipitated sulfur, or to otherwise prevent sulfur deposition, on the inside of the production tubing string as the hot oil mixes with the produced fluid and is produced up the production tubing string.
- the amount of sulfur solvent injected down the injection tubing string is substantially reduced in comparison to that used in prior art methods. This reduction is achieved because the sulfur carrying capacity of oil and produced fluids is increased at higher temperatures, because the sulfur which is formed at temperatures above the melting point of sulfur may be of such a nature that it will not readily plug the production string, and because the method will result in higher'flowing pressures which will result in less sulfur formation in the production string.
- the method results in higher flowing pressures in the production string because the reduced solvent injection requirement results in lower density fluid flowing in the tubing string. Heat transfer from the annulus into the production tubing also lowers the density of the flowing fluid and contributes to higher flowing pressures.
- the cooling associated with flashing of well fluids does not necessarily occur in the tubing string since it is possible to flow the well while maintaining minimum tubing flowing pressure above the bubble point pressure of produced fluids. Because of the lighter fluid column in the tubing 3 string wells demonstrate greater deliverability and greater ultimate recovery. At the resulting higher production rates the produced fluids contribute more of the total heat required to offset well bore heat losses and thereby reduce the amount of heat required to be injected down the circulating tubing string.
- the well 11 is provided with equipment of a type suitable for the practice of an embodiment of this invention.
- the well 11 may be completed in a conventional manner.
- a casing 12 may be run from the surface into the well to a point adjacent the bottom of the formation 10 and fixed in place with a cement 13.
- the well bore hole 14 may be opened into communication with the formation 10 by perforating the casing 12 and cement 13 with a number of perforations 15.
- a production tubing string 16 may be run into the bore hole 14 to a point adjacent the productive formation 10.
- the annular space 17 between the production tubing string 16 and the casing 12 may then be packed off above the-productive interval 10 with a suitable pack-off means such as packer 18.
- the packer 18 is preferably of a type adapted for use in dually completed wells and is preferably made from materials which are resistant to H 8 corrosion.
- a second string of tubing a hot oil injection string 9, may be extended into the well bore and connected in fluid communication with the production tubing string 16 at a point sufficiently deep to provide for the injection of hot oil-solvent into the produced fluid stream before sulfur precipitation occurs.
- the connection between the hot oil injection string 19 and the production string-16 may be made in any suitable manner. For example, if the packer 18is of the type used in dual completions, the hot oil injection string 19 maybe extended through the packer 18 thus connecting the hot oil injection string 19 in fluid communication with the packedoff interval of the bore hole 14 adjacent the formation 10 and, through the packed-off interval, into fluid communication with the production tubing string 16.
- a third tubing string may be installed in the annular space 17 between casing 12 and production tubing string 16 throughout a major length of that annulus 17 above the packer 18.
- the circulating string 20 for best results extends into the annulus 17 to a sufficient depth such that by circulating hot fluid down the circulating string 20 and p the annulus 17 the temperature of substantially all produced fluid in the production string 16 is maintained above a desired minimum which is advantageously above the melting point of sulfur.
- the circulating string 20 may be'insulated in any suitable manner.
- the circulating string 20 may comprise two concentric tubing strings 21 and 22 I with a closed annular space 23 between the strings 21 and 22.
- the annular space 23 may be filled with a low pressure gas or with other suitable insulating material.
- Insulation of circulating tubing string 20 minimizes heat transfer to the borehole 14 and surrounding earth formations as a heated fluid passes down the circulating string 20 from the'surface of the earth.
- the circulating tubing string 20 may be connected in fluid communication with a source of heated fluid such as steam source 24.
- This steam source 24 is preferably connected in fluid communication with the bore hole 14 near the earths surface, as by a conduit 224, so that fluid which flows down circulating string 20 may be returned to the steam source by flowing up the annular space 17 and through the conduit 25.
- the injection tubing string 19 may be connected at the surface in communication with a source of a solvent capable of carrying to the surface elemental sulfur which may tend to precipitate in the production tubing string 16.
- the injection tubing string may be in communication with a source of hot oil 26.
- the casing 12 is preferably closed at the surface with a suitable well head closure assembly 27.
- hydrogen sulfide-rich fluid is produced'from the formation 10 through the production tubing string 16.
- a hot fluid such as steam having a temperature about 300 F is circulated from steam source 24 down the insulated circulating string 20 and up the casing-production tubing annulus 17 in an amount sufficient to heat the produced fluid in the production tubing string and, thus, maintain the temperature of this fluid above a pre-determined minimum temperature which is advantageously above the melting point of sulfur.
- the total amount of heat required at the bottom of the circulating string 20 may be determined by considering heat losses to the equipment in the well 11 and to formations penetrated by the well as fluid moves down the circulating tubing 20 and by considering the desired minimum temperature to be maintained in the produced fluid.
- This minimum temperature which is advantageously in the range of to 250 F, is selected to minimize the amount of sulfur coming out of solution in the well annulus.
- the required temperature varies with the properties of the produced fluid. Important considerations in determining the desired minimum temperature are that the sulfur carrying capacity 'ofo il and produced fluids is increased at higher temperatures, and that sulfur formed at temperatures approaching and above the melting point may be of such a nature that it will not readily plug the production string.
- the annulus 17 is advantageously maintained at a minimum temperj ature within the range of about 180 F to about 250 F 7 along its entire length.
- a sulfur solvent for example light crude oil of about 35 API gravity heated to a temperature in the range of about 250 to 450 F, may be concurrently injected down the injection tubing string 19 from hot oil source 26 and into the packed-off interval of the bore hole 14 adjacent the formation 10.
- the fluid in the formation 10 is a liquid at prevailing conditions of temperature and pressure.
- the hot oil therefore, mixes miscibly with this produced fluid and is carried up the production tubing string 16 along with the reservoir fluid.
- the pressure and temperature of the flowing fluids may be lowered tending to cause sulfur to precipitate.
- the hot oil dissolves or otherwise carries to the surface this sulfur which might otherwise be deposited in the well bore.
- the hot oil is preferably injected down the production tubing string 16 in an amount at least sufficient to dissolve precipitated sulfur or otherwise prevent (as by providing heat to the produced fluid) sulfur deposition on the inside of the production tubing string 16 as the hot oil mixes with the produced fluid and is produced up the production tubing string 16.
- the amount of hot oil injected should be as low as possible to achieve the desired results. in many wells, injection of hot oil may not be necessary since sufficient heat to prevent sulfur deposition in the production tubing string 16 may be supplied through the circulating tubing string 20.
- a method for preventing sulfur deposition in the production tubing string of a well producing a sulfurcontaining fluid from a subterranean earth formation which comprises:
- the method of claim 1 including the step of injecting a hot sulfur-solvent into the flowing sulfurcontaining fluid through an injection tubing string connected in fluid communication with the production tubing string at a point below a pack-off means in the said well.
- a method of producing a fluid having a high hydrogen sulfide content from a fluid-containing subsurface earth formation through wells without plugging the wells with sulfur precipitate which comprises the steps of:
- step of extending an insulated tubing string into the annulus comprises extending concentric tubing strings into the annulus and filling the annular space between these concentric strings with an insulating material.
- a method for preventing sulfur deposition in the production tubing string of a well producing a sulfurcontaining fluid from a subterranean earth formation comprising the steps of;
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- Fluid Mechanics (AREA)
- Physics & Mathematics (AREA)
- Environmental & Geological Engineering (AREA)
- Geochemistry & Mineralogy (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Sulfur precipitation in the production tubing string of wells producing gas with a high hydrogen sulfide content is reduced by circulating a hot fluid down an insulated circulating tubing string and up the casing-production tubing annulus to heat produced fluid in the production tubing string and, simultaneously, injecting a hot oil into produced fluid adjacent the productive interval to dissolve precipitated sulfur and/or otherwise prevent sulfur deposition on the inside of the tubing string as the hot oil mixes with this fluid and is produced up the tubing string.
Description
United States Patent [191 Eickmeier METHOD FOR PRODUCING HIGH HYDROGEN SULFIDE CONTENT GAS WELLS [76] Inventor: James R. Eickmeier, 403 309 Eighth Ave. S.W., Calgary, Alberta, Canada 22 Filed: June 7,1972
21 Appl. No.: 260,682
[52] US. Cl. 166/303 [51] Int. Cl E211) 43/24 [58] Field of Search 166/302, 303, 57; 299/5, 299/6 [56] References Cited UNITED STATES PATENTS 3,415,573 12/1968 Fraser 299/5 X 3,451,479 6/1969 Parker 166/303 3,393,733 7/1968 Kuo et al.. 299/5 X 895,612 8/1908 Baker 166/57 [451 Mar. 12, 1974 738,326 9/1903 Higgins 166/57 UX 3,531,160 9/1970 Fisher 299/5 3,399,623 9/1968 Creed 166/302 UX 3,113,622 12/1963 Carpenter 166/302 3,410,347 11/1968 Triplett et al 166/302 X Primary ExaminerStephen J. Novosad Attorney, Agent, or FirmTom M. Moran [5 7] ABSTRACT 10 Claims, 1 Drawing Figure HOT OIL SOURCE SOURCE SOURCE PAIENIEDm 12 1974 METHOD FOR PRODUCING HIGH HYDROGEN SULFIDE CONTENT GAS WELLS BACKGROUND OF THE INVENTION hydrogen sulfide-hydrocarbon fluid flows upwardly through the tubing string the. pressure on the fluid decreases due to the reduction of the static head in the fluid column. The temperature also tends to decrease. Under these changed pressure-temperature conditions the solubility of elemental sulfur dissolved in the reservoir fluid decreases markedly and sulfur tends to come out of solution and crystalize on the tubing string causing plugging of the pipe. Plugging by sulfur deposition can become so severe as to cause stoppage of the recovery of fluids from the production well.
It has been suggested, for example see U.S. Pat No. 3,393,733 to C. H. Kuo et al, that such sulfur deposition may be prevented by injecting a hot fluid miscible with the reservoir fluid into the production tubing string near the productive interval. This injected fluid mixes with he reservoir fluids and the combined fluid is produced up the tubing string. The injected miscible liquid dissolves sulfur as it forms in the tubing or by other means prevents sulfur-from depositing on the tubing. Injected fluid temperature and rate are determined to satisfy the condition that injected fluid take into solution, or otherwise transport to the surface, all sulfur which precipitates in the tubing.
This prior art production technique has the disadvantage that injected fluid, which is generally more dense than produced fluid, is required in such quantity as to significantly increase the pressure gradient in the tubing string. This imposes an increased back-pressure on the productive formation and results in decreased well deliverability. In addition, the large amount of elemental sulfur contained in the injected fluid must be separated from that fluid at the surfaceif the sulfur is to be recovered or if the solvent is to be reused. This may require a substantial amount of separating equipment and attendant expense.
SUMMARY OF THE INVENTION It has now been found that sulfur-containing fluid' can be produced from a subsurface formation without plugging of the production tubing from sulfur deposition by flowing the fluid to the surface through a production tubing string while heating the flowing sulfurcontaining fluid indirectly by heating the production tubing string and thereby conductively heating the flowing fluid. For example, heat may be supplied to the production tubing string from electric heating coils disposed around the tubing string or by circulating a hot fluid into the well and into contact with the exterior of the production tubing string. The flowing sulfurcontaining fluid may be concurrently heated directly by injecting a hot sulfur-solvent into the well and into contact with the produced sulfur-containing fluid.
According to a specific embodiment of the method of invention, a well bore extending from the surface to a formation of interest containing a fluid having a high hydrogen sulfide content is at least partially lined with a large diameter tubular casing and is completed so as to be in fluid communication with the formation. A first string of tubing, a production tubing string, is then extended into the well to a point adjacent the bottom of the productive formation. The casing-production tubing string annulus is packed off with a pack-off means set above the productive formation and a second string of tubing, a hot-oil injection string, is extended into the well bore and through the pack-off means to connect this hot oil injection string in fluidcommunication with the packed-off interval of the well bore opposite the productive formation. A third string of tubing, an insulated circulating string, is then installed in the casingproduction tubing annulus so as to extend throughout a major length of the annulus above the pack-off means. i
Hydrogen sulfide rich fluid may. than be produced from the productive formation through the production tubing string. Simultaneously, a hot fluid, such as steam having a temperature about 300 F, is circulated down the insulated circulating tubing string and up the casing-production tubing annulus in an amount sufficient to heat the produced fluid in the production tubing string and thereby maintain the temperature of this fluid above a pre-detennined minimum temperature, which is preferably above the melting point of sulfur. Concurrently, a fluid in which sulfur is soluble, such as a light substantially sulfur-free crude oil, advantageously can be injected down the injection tubing string into the packed-off interval of the well bore and produced up the production tubing string with the reservoir fluid in an amount sufficient to dissolve precipitated sulfur, or to otherwise prevent sulfur deposition, on the inside of the production tubing string as the hot oil mixes with the produced fluid and is produced up the production tubing string.
When operating according to this method the amount of sulfur solvent injected down the injection tubing string is substantially reduced in comparison to that used in prior art methods. This reduction is achieved because the sulfur carrying capacity of oil and produced fluids is increased at higher temperatures, because the sulfur which is formed at temperatures above the melting point of sulfur may be of such a nature that it will not readily plug the production string, and because the method will result in higher'flowing pressures which will result in less sulfur formation in the production string.
The method results in higher flowing pressures in the production string because the reduced solvent injection requirement results in lower density fluid flowing in the tubing string. Heat transfer from the annulus into the production tubing also lowers the density of the flowing fluid and contributes to higher flowing pressures.
At these higher flowing pressures, the cooling associated with flashing of well fluids does not necessarily occur in the tubing string since it is possible to flow the well while maintaining minimum tubing flowing pressure above the bubble point pressure of produced fluids. Because of the lighter fluid column in the tubing 3 string wells demonstrate greater deliverability and greater ultimate recovery. At the resulting higher production rates the produced fluids contribute more of the total heat required to offset well bore heat losses and thereby reduce the amount of heat required to be injected down the circulating tubing string.
BRIEF DESCRIPTION OF THE DRAWING The Drawing shows a view, partly in cross-section, of an earth formation penetrated by a well suitably equipped for the practice of this invention.
DESCRIPTION OF PREFERRED EMBODIMENT Referring to the drawing, we see a subsurface, fluidcontaining earth formation penetrated by a well 11. The well 11 is provided with equipment of a type suitable for the practice of an embodiment of this invention. The well 11 may be completed in a conventional manner. For example, a casing 12 may be run from the surface into the well to a point adjacent the bottom of the formation 10 and fixed in place with a cement 13. The well bore hole 14 may be opened into communication with the formation 10 by perforating the casing 12 and cement 13 with a number of perforations 15.
t To produce a fluid having a high hydrogen sulfide content from the formation 10 according to this embodiment of the invention, a production tubing string 16 may be run into the bore hole 14 to a point adjacent the productive formation 10. The annular space 17 between the production tubing string 16 and the casing 12 may then be packed off above the-productive interval 10 with a suitable pack-off means such as packer 18. The packer 18 is preferably of a type adapted for use in dually completed wells and is preferably made from materials which are resistant to H 8 corrosion.
A second string of tubing, a hot oil injection string 9, may be extended into the well bore and connected in fluid communication with the production tubing string 16 at a point sufficiently deep to provide for the injection of hot oil-solvent into the produced fluid stream before sulfur precipitation occurs. The connection between the hot oil injection string 19 and the production string-16 may be made in any suitable manner. For example, if the packer 18is of the type used in dual completions, the hot oil injection string 19 maybe extended through the packer 18 thus connecting the hot oil injection string 19 in fluid communication with the packedoff interval of the bore hole 14 adjacent the formation 10 and, through the packed-off interval, into fluid communication with the production tubing string 16.
A third tubing string, advantageously, an insulatedcirculating string 20 may be installed in the annular space 17 between casing 12 and production tubing string 16 throughout a major length of that annulus 17 above the packer 18. The circulating string 20 for best results extends into the annulus 17 to a sufficient depth such that by circulating hot fluid down the circulating string 20 and p the annulus 17 the temperature of substantially all produced fluid in the production string 16 is maintained above a desired minimum which is advantageously above the melting point of sulfur.
The circulating string 20 may be'insulated in any suitable manner. For example, the circulating string 20 may comprise two concentric tubing strings 21 and 22 I with a closed annular space 23 between the strings 21 and 22. The annular space 23 may be filled with a low pressure gas or with other suitable insulating material.
Insulation of circulating tubing string 20 minimizes heat transfer to the borehole 14 and surrounding earth formations as a heated fluid passes down the circulating string 20 from the'surface of the earth. The circulating tubing string 20 may be connected in fluid communication with a source of heated fluid such as steam source 24. This steam source 24 is preferably connected in fluid communication with the bore hole 14 near the earths surface, as by a conduit 224, so that fluid which flows down circulating string 20 may be returned to the steam source by flowing up the annular space 17 and through the conduit 25.
The injection tubing string 19 may be connected at the surface in communication with a source of a solvent capable of carrying to the surface elemental sulfur which may tend to precipitate in the production tubing string 16. For example, the injection tubing string may be in communication with a source of hot oil 26. The casing 12 is preferably closed at the surface with a suitable well head closure assembly 27.
-According to this embodiment of the invention, hydrogen sulfide-rich fluid is produced'from the formation 10 through the production tubing string 16. Simultaneously, a hot fluid such as steam having a temperature about 300 F is circulated from steam source 24 down the insulated circulating string 20 and up the casing-production tubing annulus 17 in an amount sufficient to heat the produced fluid in the production tubing string and, thus, maintain the temperature of this fluid above a pre-determined minimum temperature which is advantageously above the melting point of sulfur. The total amount of heat required at the bottom of the circulating string 20 may be determined by considering heat losses to the equipment in the well 11 and to formations penetrated by the well as fluid moves down the circulating tubing 20 and by considering the desired minimum temperature to be maintained in the produced fluid.
This minimum temperature, which is advantageously in the range of to 250 F, is selected to minimize the amount of sulfur coming out of solution in the well annulus. The required temperature, of course, varies with the properties of the produced fluid. Important considerations in determining the desired minimum temperature are that the sulfur carrying capacity 'ofo il and produced fluids is increased at higher temperatures, and that sulfur formed at temperatures approaching and above the melting point may be of such a nature that it will not readily plug the production string. To maintain the desired minimum the annulus 17 is advantageously maintained at a minimum temperj ature within the range of about 180 F to about 250 F 7 along its entire length.
To supplement heat circulated down the circulating tubing string 20, a sulfur solvent, for example light crude oil of about 35 API gravity heated to a temperature in the range of about 250 to 450 F, may be concurrently injected down the injection tubing string 19 from hot oil source 26 and into the packed-off interval of the bore hole 14 adjacent the formation 10. In many wells the fluid in the formation 10 is a liquid at prevailing conditions of temperature and pressure. The hot oil, therefore, mixes miscibly with this produced fluid and is carried up the production tubing string 16 along with the reservoir fluid. As the mixture of fluids moves up the production tubing string 16, the pressure and temperature of the flowing fluids may be lowered tending to cause sulfur to precipitate. The hot oil dissolves or otherwise carries to the surface this sulfur which might otherwise be deposited in the well bore. Therefore, the hot oil is preferably injected down the production tubing string 16 in an amount at least sufficient to dissolve precipitated sulfur or otherwise prevent (as by providing heat to the produced fluid) sulfur deposition on the inside of the production tubing string 16 as the hot oil mixes with the produced fluid and is produced up the production tubing string 16. However, in order to reduce the increased fluid pressure gradient in the production tubing string 16 caused by the relatively high density hot oil, the amount of hot oil injected should be as low as possible to achieve the desired results. in many wells, injection of hot oil may not be necessary since sufficient heat to prevent sulfur deposition in the production tubing string 16 may be supplied through the circulating tubing string 20.
By reducing injection of hot oil and by heating fluid in the production tubing string 16, operating according to the present invention provides a produced fluid column lighter than that obtained in prior art production methods. This results in higher flowing pressures in the tubing 16. At such higher flowing'pressures the considerable cooling associated with the flashing of produced fluid from the liquid to the gas phase may not occur in the tubing string 16. It may be possible to flow the well 11 while maintaining minimum flowing pressure throughout the production tubing string 16 above the bubble point pressure of the reservoir fluid. This significantly reduces the precipitation of sulfur in the well 11. Additionally, the well 11 may demonstrate greater deliverability and greater ultimate flowing recovery as a result of the lighter fluid column in the tubing string. Also, injected heat requirements are reduced since reservoir fluids are produced more rapidly and therefore lose less heat to the well 11.
The embodiment of the invention in which an exclusive property or previlege is claimed are defined as follows:
1. A method for preventing sulfur deposition in the production tubing string of a well producing a sulfurcontaining fluid from a subterranean earth formation which comprises:
flowing the sulfur-containing fluid from the earth formation to the surface through the production tubing string; and
simultaneously heating the production tubing string by circulating a heated fluid into the well through an insulated string of pipe and up the casingproduction tubing annulus to thereby indirectly heat the flowing sulfur-containing fluid in the production tubing string. v
2. The method of claim 1 where the hot fluid is steam.
3. The method of claim 1 where the heated fluid has a temperature sufficient to maintain the temperature of the flowing sulfur-containing fluid above the melting point of sulfur.
4. The method of claim 1 including the step of injecting a hot sulfur-solvent into the flowing sulfurcontaining fluid through an injection tubing string connected in fluid communication with the production tubing string at a point below a pack-off means in the said well.
5. The method of claim 4 where the hot sulfursolvent is a heated light crude oil.
6. The method of claim 4 wherein the hot sulfursolvent is heated to a temperature in the range of 250 to 450 F.
7. A method of producing a fluid having a high hydrogen sulfide content from a fluid-containing subsurface earth formation through wells without plugging the wells with sulfur precipitate which comprises the steps of:
providing a well bore extending from the earth surface to the subsurface earth formation;
lining at least a part of the well bore with a tubular casing; completing the well bore in fluid communication with the subsurface earth formation;
extending a production tubing string into the wellbore to a point adajacent the subsurface earth formation whereby an annulus is defined between the tubular casing and the production string of tubing;
packing off the annulus with a pack off means set at a point in the well bore above the subsurface earth formation to prevent fluid flow up the annulus from the subsurface earth formation; extending an insulated circulating tubing string into the annulus to a point above the pack off means;
producing fluid having a high hydrogen sulfide content up the production tubing string from the subsurface earth formation;
and simultaneously circulating a hot fluid down the insulated circulating string and up the annulus to heat the produced fluid in the production tubing string and thereby retard sulfur precipitation in the production tubing string 8. The method of claim 7 including the steps of:
extending an injection tubing string into the well bore;
connecting the injection tubing string in fluid communication with the production tubing string at a point adjacent the top of the subsurface earth formation; and
injecting a hot sulfur-solvent down the injection tubing string whereby the hot sulfur-solvent mixes with the produced fluid in the production tubing string and is produced up the production tubing string along with the produced fluid to carry to the surface sulfur which may precipitate from the produced fluid in the production tubing string.
9. The method of claim 7 wherein the step of extending an insulated tubing string into the annulus comprises extending concentric tubing strings into the annulus and filling the annular space between these concentric strings with an insulating material.
10. A method for preventing sulfur deposition in the production tubing string of a well producing a sulfurcontaining fluid from a subterranean earth formation comprising the steps of;
flowing the sulfur-containing fluid from the production zone to the surface through the production tubing string;
heating the outside of the production tubing string to heat the sulfur-containing fluid flowing through the production tubing string to retard sulfur deposition from the flowing fluid; and
injecting a hot sulfur-solvent into the flowing sulfurcontaining fluid through an injection tubing string at a point below a pack-off means in said well. a:
3, 3? UNITED STATES PATENT QFFICE CERTIFICATE OF CORRECTION Patent No. 3,796,265 Dated March 12 1974 I JAMES R. EICKMEIER It: is certified that error appears inthe above-identified patent and that said Letters Patentare hereby corrected as shown below:
r- The Patent should read:
"[30] Foreign Application Priority August 19, 1971, Canada 120,935"
Signed and sealed this 22nd day of October 1974.
Y SEAL) I Attest McCOY M. GIBSONIJR. C. MARSHALL DANN Attesting Officer Commissioner of Patents
Claims (9)
- 2. The method of claim 1 where the hot fluid is steam.
- 3. The method of claim 1 where the heated fluid has a temperature sufficient to maintain the temperature of the flowing sulfur-containing fluid above the melting point of sulfur.
- 4. The method of claim 1 including the step of injecting a hot sulfur-solvent into the flowing sulfur-containing fluid through an injection tubing string connected in fluid communication with the production tubing string at a point below a pack-off means in the said well.
- 5. The method of claim 4 where the hot sulfur-solvent is a heated light crude oil.
- 6. The method of claim 4 wherein the hot sulfur-solvent is heated to a temperature in the range of 250* to 450* F.
- 7. A method of producing a fluid having a high hydrogen sulfide content from a fluid-containing subsurface earth formation through wells without plugging the wells with sulfur precipitate which comprises the steps of: providing a well bore extending from the earth surface to the subsurface earth formation; lining at least a part of the well bore with a tubular casing; completing the well bore in fluid communication with the subsurface earth formation; extending a production tubing string into the wellbore to a point adajacent the subsurface earth formation whereby an annulus is defined between the tubular casing and the production string of tubing; packing off the annulus with a pack off means set at a point in the well bore above the subsurface earth formation to prevent fluid flow up the annulus from the subsurface earth formation; extending an insulated circulating tubing string into the annulus to a point above the pack off means; producing fluid having a high hydrogen sulfide content up the production tubing string from the subsurface earth formation; and simultaneously circulating a hot fluid down the insulated circulating string and up the annulus to heat the produced fluid in the production tubing string and thereby retard sulfur precipitation in the production tubing string
- 8. The method of claim 7 including the steps of: extending an injection tubing string into the well bore; connecting the injection tubing stRing in fluid communication with the production tubing string at a point adjacent the top of the subsurface earth formation; and injecting a hot sulfur-solvent down the injection tubing string whereby the hot sulfur-solvent mixes with the produced fluid in the production tubing string and is produced up the production tubing string along with the produced fluid to carry to the surface sulfur which may precipitate from the produced fluid in the production tubing string.
- 9. The method of claim 7 wherein the step of extending an insulated tubing string into the annulus comprises extending concentric tubing strings into the annulus and filling the annular space between these concentric strings with an insulating material.
- 10. A method for preventing sulfur deposition in the production tubing string of a well producing a sulfur-containing fluid from a subterranean earth formation comprising the steps of; flowing the sulfur-containing fluid from the production zone to the surface through the production tubing string; heating the outside of the production tubing string to heat the sulfur-containing fluid flowing through the production tubing string to retard sulfur deposition from the flowing fluid; and injecting a hot sulfur-solvent into the flowing sulfur-containing fluid through an injection tubing string at a point below a pack-off means in said well.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US26068272A | 1972-06-07 | 1972-06-07 |
Publications (1)
Publication Number | Publication Date |
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US3796265A true US3796265A (en) | 1974-03-12 |
Family
ID=22990174
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US00260682A Expired - Lifetime US3796265A (en) | 1972-06-07 | 1972-06-07 | Method for producing high hydrogen sulfide content gas wells |
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3952802A (en) * | 1974-12-11 | 1976-04-27 | In Situ Technology, Inc. | Method and apparatus for in situ gasification of coal and the commercial products derived therefrom |
US4008765A (en) * | 1975-12-22 | 1977-02-22 | Chevron Research Company | Method of recovering viscous petroleum from thick tar sand |
US4019575A (en) * | 1975-12-22 | 1977-04-26 | Chevron Research Company | System for recovering viscous petroleum from thick tar sand |
US5238066A (en) * | 1992-03-24 | 1993-08-24 | Exxon Production Research Company | Method and apparatus for improved recovery of oil and bitumen using dual completion cyclic steam stimulation |
CN105954216A (en) * | 2016-04-28 | 2016-09-21 | 浙江大学 | Method for measuring concentration of silicate in high-concentration hydrogen sulfide hydrothermal solution |
CN105973819A (en) * | 2016-04-28 | 2016-09-28 | 浙江大学 | Method for determining concentration of phosphate in high-concentration hydrogen sulfide hot liquid |
CN106968639A (en) * | 2017-03-13 | 2017-07-21 | 中国石油化工股份有限公司 | A kind of method of hydrogen sulfide in improvement oil well |
CN110108444A (en) * | 2019-04-28 | 2019-08-09 | 辽宁石油化工大学 | A kind of sulfur-containing gas pipeline sulphur sedimentation experiment device |
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US895612A (en) * | 1902-06-11 | 1908-08-11 | Delos R Baker | Apparatus for extracting the volatilizable contents of sedimentary strata. |
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Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
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US3952802A (en) * | 1974-12-11 | 1976-04-27 | In Situ Technology, Inc. | Method and apparatus for in situ gasification of coal and the commercial products derived therefrom |
US4008765A (en) * | 1975-12-22 | 1977-02-22 | Chevron Research Company | Method of recovering viscous petroleum from thick tar sand |
US4019575A (en) * | 1975-12-22 | 1977-04-26 | Chevron Research Company | System for recovering viscous petroleum from thick tar sand |
US5238066A (en) * | 1992-03-24 | 1993-08-24 | Exxon Production Research Company | Method and apparatus for improved recovery of oil and bitumen using dual completion cyclic steam stimulation |
CN105954216A (en) * | 2016-04-28 | 2016-09-21 | 浙江大学 | Method for measuring concentration of silicate in high-concentration hydrogen sulfide hydrothermal solution |
CN105973819A (en) * | 2016-04-28 | 2016-09-28 | 浙江大学 | Method for determining concentration of phosphate in high-concentration hydrogen sulfide hot liquid |
CN105954216B (en) * | 2016-04-28 | 2019-02-05 | 浙江大学 | The measuring method of silicate concentration in high-concentration hydrogen sulfide hydrothermal solution |
CN105973819B (en) * | 2016-04-28 | 2019-02-19 | 浙江大学 | The measuring method of phosphate concn in high-concentration hydrogen sulfide hydrothermal solution |
CN106968639A (en) * | 2017-03-13 | 2017-07-21 | 中国石油化工股份有限公司 | A kind of method of hydrogen sulfide in improvement oil well |
CN106968639B (en) * | 2017-03-13 | 2018-06-29 | 中国石油化工股份有限公司 | A kind of method of hydrogen sulfide in improvement oil well |
CN110108444A (en) * | 2019-04-28 | 2019-08-09 | 辽宁石油化工大学 | A kind of sulfur-containing gas pipeline sulphur sedimentation experiment device |
CN110108444B (en) * | 2019-04-28 | 2020-12-01 | 辽宁石油化工大学 | Sulfur deposition experimental device for sulfur-containing natural gas pipeline |
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