CA2407554C - Method and apparatus for desanding wellhead production - Google Patents
Method and apparatus for desanding wellhead production Download PDFInfo
- Publication number
- CA2407554C CA2407554C CA002407554A CA2407554A CA2407554C CA 2407554 C CA2407554 C CA 2407554C CA 002407554 A CA002407554 A CA 002407554A CA 2407554 A CA2407554 A CA 2407554A CA 2407554 C CA2407554 C CA 2407554C
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- particulates
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- 238000000034 method Methods 0.000 title claims description 12
- 238000004519 manufacturing process Methods 0.000 title description 8
- 239000012530 fluid Substances 0.000 claims abstract description 133
- 230000004888 barrier function Effects 0.000 claims abstract description 24
- 210000001015 abdomen Anatomy 0.000 claims abstract description 20
- 239000000725 suspension Substances 0.000 claims abstract description 8
- 238000009825 accumulation Methods 0.000 claims abstract 4
- 230000000737 periodic effect Effects 0.000 claims abstract 2
- 238000004140 cleaning Methods 0.000 claims description 4
- 238000003860 storage Methods 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 2
- 238000007599 discharging Methods 0.000 claims 7
- 239000003208 petroleum Substances 0.000 claims 3
- 230000035508 accumulation Effects 0.000 abstract 1
- 239000004576 sand Substances 0.000 description 15
- 230000003628 erosive effect Effects 0.000 description 4
- 239000000835 fiber Substances 0.000 description 4
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 241001527902 Aratus Species 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 241000237858 Gastropoda Species 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 230000003466 anti-cipated effect Effects 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
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
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/34—Arrangements for separating materials produced by the well
- E21B43/35—Arrangements for separating materials produced by the well specially adapted for separating solids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2221/00—Applications of separation devices
- B01D2221/04—Separation devices for treating liquids from earth drilling, mining
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- Geology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Mining & Mineral Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- Physics & Mathematics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Gas Separation By Absorption (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Separating Particles In Gases By Inertia (AREA)
- Treating Waste Gases (AREA)
Abstract
A desanding vessel is connected to a fluid stream containing entrained particulates flowing from a wellhead. The vessel comprises an upper freeboard volume wherein the fluid velocity drops and particulates fall from suspension. Preferably the fluid stream is introduced offset upwardly from an axis of a horizontally-oriented cylindrical vessel, released particulates falling to accumulate in a lower belly portion. The freeboard volume is maintained using a depending flow barrier spaced from the fluid inlet and adjacent the vessel's outlet. A cleanout enables periodic removal of accumulations.
Description
1 "METHOD AND APF~ARATUS FOR
2 DESANDING WELLHEAD PRODUCTION"
3
4 FIELD OF THE INVENTION
The present invention relates i:o apparatus and methodology for the 6 removal of particulates such as sand from fluid streams produced from a well while 7 minimizing erosion of the involved equipment.
Production from wells in the oil and gas industry often contains 11 particulates. These particulates could be part of the formation from which the 12 hydrocarbon is being produced, introduced ~>articulates from hydraulic fracturing or 13 fluid loss material from drilling mud or fracturing fluids or from a phase changes of 14 produced hydrocarbons caused by changing conditions at the wellbore (asphalt or wax formation). As the particulates are produced, problems occur due to abrasion, 16 and plugging of production equipment. In a typical startup after fracturing, a 17 stimulated well may produce sand until the ~Nell has stabilized, sometimes up to a 18 month.
19 In the case of gas wells, fluid velocities can be high enough that the erosion of the production equipment is severe enough to cause catastrophic failure.
21 High velocities are typical and are even designed for elutriating particles up the well 22 and to the surface. An erosive failure of this nature can become a serious safety 23 and environmental issue for the well operator. In all cases, particulate production 1 contaminates surface equipment and produced fluids and impairs the normal 2 operation of the oil and gas gathering system and process facilities.
3 In one prior art system, a pressurized tank ("P Tank") is placed on the 4 wellsite and the well is allowed to produce f'uid and particulates into this tank until sand production ceases. The large size of v:he tank usually restricts the maximum 6 operating pressure of the vessel to somethirn~ in the order of 1,000 - 2,100 kPa. In 7 the case of a gas well, this requires some pressure control to be placed on the well 8 to protect the P Tank. Further, for a gas ~Nell, the pressure reduction usually is 9 associated with an increase in gas velocity which in turn makes the sand laden well effluent much more abrasive. Other problems associated with this type of desanding 11 technique are that it is a temporary solution. If the well continues to make sand, the 12 solution becomes prohibitively expensive. In most situations with this kind of 13 temporary solution, the gas vapors are not conserved and sold as a commercial 14 product.
An alternate known prior art system includes employing filters to 16 remove particulates. A common design is ':o have a number of fibre mesh bags 17 placed inside a pressure vessel. The fibre density is matched to the anticipated 18 particulate size. Filter bags are generally not effective in the removal of particulates 19 in a multiphase conditions. Usually multipha:~e flow in the oil and gas operations is unstable. Large slugs of fluid followed by a g~~s mist is common. In these cases, the 21 fibre bags become a pressure drop point and often fail due to the liquid flow through 22 filter. Due to the high chance of failure, the filter may not be trusted to remove 23 particulates in critical applications or where the flow parameters of a well are 1 unknown. An additional problem with filters in most jurisdictions is associated with 2 cost of disposal. The fibre bags are considered to be contaminated with 3 hydrocarbons and must be disposed of in accordance to local environmental 4 regulations.
Clearly there is a need for more versatile and cost effective system.
7 SUMMARY OF THE. INVENTION
8 Apparatus is provided which is placed adjacent to the wellhead for 9 intercepting wellhead fluid flow before and prior to entry to any operators equipment including separators, valves, chokes and all other downstream equipment.
11 A pressure vessel is inserted in the flowsteam by connecting it 12 adjacent to the wellhead and to the input high velocity field piping extending from the 13 wellhead. The vessel contains a freeboard volume having a cross-sectional area 14 which is greater than that of the field piping i~rom whence the fluids emanate. As a result, fluid velocity drops and particulates cannot be maintained in suspension. The 16 freeboard cross-sectional area is maintained through a downcomer weir or 17 depending nozzle at the vessel's exit which ensures that a minimum freeboard 18 volume and cross-sectional area is maintained for the collection of particulates, and 19 promotes maximum use of the freeboard area, thereby reducing the number of times maintenance of the system, by cleaning the freeboard area of accumulated 21 particulates, need be conducted.
2 Figure 1 is a cross-sectional side view of one embodiment of the 3 invention;
4 Figure 2 is a typical installation for wellsite service, such as that provided on a portable trailer; and 6 Figure 3 is a performance graph of the achievable gas rates while 7 still achieving particulate removal.
As shown in Fig. 1, a desander 10 comprises a substantially 11 horizontal, cylindrical, pressure vessel 11 having an inlet end 23 adapted for 12 connection to a wellhead piping 9 and fluid stream F, typically gas G and sand S.
13 As stated in the background and below, the fluid stream F may also contain liquid 14 L.
A fluid inlet 12 comprises a nozzle 21 extending into an upper 16 freeboard 30 volume adjacent the top of the vessel 11. An eccentric fitting 17 shifts the axis A of the vessel 11 downward to form a belly storage portion 32 for 18 receiving and temporarily storing sand S. The nozzle 21 extends beyond the end 19 of the vessel 11 and into the freeboard 30 which minimizes localized wear.
Gas G containing sand S enters through the fluid inlet 12 and is received by a 21 larger cross-sectional area of the freeboard 30. The velocity slows and sand falls 22 out of suspension. The freeboard 30 is maintained using means to ensure that 23 the particulate free fluid is collected by an outlet 13 from mid-vessel.
1 This is achieved using either flow barrier such as a weir 40 as shown or by inserting 2 the fluid outlet into the vessel 11, away from the vessel wall.
3 As shown in Fig. 1, if a weir 40 is used, it is spaced from the fluid inlet 4 12 and positioned between the fluid inlet 12 and the fluid outlet 13.
As shown in Fig. 1, both a wE:ir 40, and a fluid outlet 13, having a 6 downwardly extending portion which extends into the vessel 11, are used as a flow 7 barrier in a preferred embodiment.
8 The fluid outlet 13 for the ves,el 11 is preferably perpendicular and 9 upward, drawing from the lower level of the freeboard 30 volume.
A quick release pressure-vessel compatible cleanout 50 is provided for 11 sand removal access. The vessel 11 must be depressurized before opening and 12 cleaning out particulates. Manual cleanout is performed although automated 13 cleanout could be incorporated without diverging from the intent of the invention.
14 A typical vessel 11 may be a 6" diameter, schedule 160 shell having a capacity for 8 million cubic feet of gas G per day and a corresponding and typical 16 collection rate of 1.5 gallons of particulates pE~r day.
17 The advantages of the system include:
18 ~ As the desander is more cost effective than a "P Tank", the 19 desander can be economically placed on a well for long term (substantially permanent) sand protection;
21 ~ With a pressure rating that allows it to operate at the wells 22 conditions, minimal pressure drop is experienced across the 23 vessel. The desander i > designed to exceed ASME code for
The present invention relates i:o apparatus and methodology for the 6 removal of particulates such as sand from fluid streams produced from a well while 7 minimizing erosion of the involved equipment.
Production from wells in the oil and gas industry often contains 11 particulates. These particulates could be part of the formation from which the 12 hydrocarbon is being produced, introduced ~>articulates from hydraulic fracturing or 13 fluid loss material from drilling mud or fracturing fluids or from a phase changes of 14 produced hydrocarbons caused by changing conditions at the wellbore (asphalt or wax formation). As the particulates are produced, problems occur due to abrasion, 16 and plugging of production equipment. In a typical startup after fracturing, a 17 stimulated well may produce sand until the ~Nell has stabilized, sometimes up to a 18 month.
19 In the case of gas wells, fluid velocities can be high enough that the erosion of the production equipment is severe enough to cause catastrophic failure.
21 High velocities are typical and are even designed for elutriating particles up the well 22 and to the surface. An erosive failure of this nature can become a serious safety 23 and environmental issue for the well operator. In all cases, particulate production 1 contaminates surface equipment and produced fluids and impairs the normal 2 operation of the oil and gas gathering system and process facilities.
3 In one prior art system, a pressurized tank ("P Tank") is placed on the 4 wellsite and the well is allowed to produce f'uid and particulates into this tank until sand production ceases. The large size of v:he tank usually restricts the maximum 6 operating pressure of the vessel to somethirn~ in the order of 1,000 - 2,100 kPa. In 7 the case of a gas well, this requires some pressure control to be placed on the well 8 to protect the P Tank. Further, for a gas ~Nell, the pressure reduction usually is 9 associated with an increase in gas velocity which in turn makes the sand laden well effluent much more abrasive. Other problems associated with this type of desanding 11 technique are that it is a temporary solution. If the well continues to make sand, the 12 solution becomes prohibitively expensive. In most situations with this kind of 13 temporary solution, the gas vapors are not conserved and sold as a commercial 14 product.
An alternate known prior art system includes employing filters to 16 remove particulates. A common design is ':o have a number of fibre mesh bags 17 placed inside a pressure vessel. The fibre density is matched to the anticipated 18 particulate size. Filter bags are generally not effective in the removal of particulates 19 in a multiphase conditions. Usually multipha:~e flow in the oil and gas operations is unstable. Large slugs of fluid followed by a g~~s mist is common. In these cases, the 21 fibre bags become a pressure drop point and often fail due to the liquid flow through 22 filter. Due to the high chance of failure, the filter may not be trusted to remove 23 particulates in critical applications or where the flow parameters of a well are 1 unknown. An additional problem with filters in most jurisdictions is associated with 2 cost of disposal. The fibre bags are considered to be contaminated with 3 hydrocarbons and must be disposed of in accordance to local environmental 4 regulations.
Clearly there is a need for more versatile and cost effective system.
7 SUMMARY OF THE. INVENTION
8 Apparatus is provided which is placed adjacent to the wellhead for 9 intercepting wellhead fluid flow before and prior to entry to any operators equipment including separators, valves, chokes and all other downstream equipment.
11 A pressure vessel is inserted in the flowsteam by connecting it 12 adjacent to the wellhead and to the input high velocity field piping extending from the 13 wellhead. The vessel contains a freeboard volume having a cross-sectional area 14 which is greater than that of the field piping i~rom whence the fluids emanate. As a result, fluid velocity drops and particulates cannot be maintained in suspension. The 16 freeboard cross-sectional area is maintained through a downcomer weir or 17 depending nozzle at the vessel's exit which ensures that a minimum freeboard 18 volume and cross-sectional area is maintained for the collection of particulates, and 19 promotes maximum use of the freeboard area, thereby reducing the number of times maintenance of the system, by cleaning the freeboard area of accumulated 21 particulates, need be conducted.
2 Figure 1 is a cross-sectional side view of one embodiment of the 3 invention;
4 Figure 2 is a typical installation for wellsite service, such as that provided on a portable trailer; and 6 Figure 3 is a performance graph of the achievable gas rates while 7 still achieving particulate removal.
As shown in Fig. 1, a desander 10 comprises a substantially 11 horizontal, cylindrical, pressure vessel 11 having an inlet end 23 adapted for 12 connection to a wellhead piping 9 and fluid stream F, typically gas G and sand S.
13 As stated in the background and below, the fluid stream F may also contain liquid 14 L.
A fluid inlet 12 comprises a nozzle 21 extending into an upper 16 freeboard 30 volume adjacent the top of the vessel 11. An eccentric fitting 17 shifts the axis A of the vessel 11 downward to form a belly storage portion 32 for 18 receiving and temporarily storing sand S. The nozzle 21 extends beyond the end 19 of the vessel 11 and into the freeboard 30 which minimizes localized wear.
Gas G containing sand S enters through the fluid inlet 12 and is received by a 21 larger cross-sectional area of the freeboard 30. The velocity slows and sand falls 22 out of suspension. The freeboard 30 is maintained using means to ensure that 23 the particulate free fluid is collected by an outlet 13 from mid-vessel.
1 This is achieved using either flow barrier such as a weir 40 as shown or by inserting 2 the fluid outlet into the vessel 11, away from the vessel wall.
3 As shown in Fig. 1, if a weir 40 is used, it is spaced from the fluid inlet 4 12 and positioned between the fluid inlet 12 and the fluid outlet 13.
As shown in Fig. 1, both a wE:ir 40, and a fluid outlet 13, having a 6 downwardly extending portion which extends into the vessel 11, are used as a flow 7 barrier in a preferred embodiment.
8 The fluid outlet 13 for the ves,el 11 is preferably perpendicular and 9 upward, drawing from the lower level of the freeboard 30 volume.
A quick release pressure-vessel compatible cleanout 50 is provided for 11 sand removal access. The vessel 11 must be depressurized before opening and 12 cleaning out particulates. Manual cleanout is performed although automated 13 cleanout could be incorporated without diverging from the intent of the invention.
14 A typical vessel 11 may be a 6" diameter, schedule 160 shell having a capacity for 8 million cubic feet of gas G per day and a corresponding and typical 16 collection rate of 1.5 gallons of particulates pE~r day.
17 The advantages of the system include:
18 ~ As the desander is more cost effective than a "P Tank", the 19 desander can be economically placed on a well for long term (substantially permanent) sand protection;
21 ~ With a pressure rating that allows it to operate at the wells 22 conditions, minimal pressure drop is experienced across the 23 vessel. The desander i > designed to exceed ASME code for
5 1 pressure vessels. This permits the sand to be removed from 2 the flow stream without becoming erosive.
3 ~ Since the vessel is passive and has no moving parts, plugging 4 caused by particulates is not an issue. Sand is removed mechanically from the vE;ssel at regular intervals. By removing
3 ~ Since the vessel is passive and has no moving parts, plugging 4 caused by particulates is not an issue. Sand is removed mechanically from the vE;ssel at regular intervals. By removing
6 the sand prior to it entering the producing system, contamination
7 of equipment and produced fluids is avoided.
8 . The vessel is capable of handling multiphase production and
9 has demonstrated the a~~ility to remove sand from both gas and oil streams. This result: in a wider application than the filter 11 methods.
Claims (34)
EXCLUSIVE PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS
FOLLOWS:
1. A desanding vessel for removing particulates in a fluid stream, comprising:
a fluid inlet adjacent a first end of the vessel and adapted for receiving the fluid stream, the fluid inlet discharging the fluid stream at an inlet velocity into a freeboard portion at a top of the vessel, the fluid stream in the freeboard portion having a cross-sectional area greater than that of the inlet for creating a freeboard velocity less than the inlet velocity such that contained particulates fall out of suspension;
a fluid outlet from the vessel, the fluid outlet being spaced horizontally from the fluid inlet; and a flow barrier, depending from the top of the vessel and having a lower edge so as to direct the fluid stream below the flow barrier before the fluid stream discharges from the fluid outlet for maintaining the freeboard portion and forming a belly storage portion therebelow, the flow barrier further being positioned between the fluid inlet and fluid outlet and spaced from the fluid inlet so as to cause accumulation of particulates in the belly portion prior to the flow barrier.
a fluid inlet adjacent a first end of the vessel and adapted for receiving the fluid stream, the fluid inlet discharging the fluid stream at an inlet velocity into a freeboard portion at a top of the vessel, the fluid stream in the freeboard portion having a cross-sectional area greater than that of the inlet for creating a freeboard velocity less than the inlet velocity such that contained particulates fall out of suspension;
a fluid outlet from the vessel, the fluid outlet being spaced horizontally from the fluid inlet; and a flow barrier, depending from the top of the vessel and having a lower edge so as to direct the fluid stream below the flow barrier before the fluid stream discharges from the fluid outlet for maintaining the freeboard portion and forming a belly storage portion therebelow, the flow barrier further being positioned between the fluid inlet and fluid outlet and spaced from the fluid inlet so as to cause accumulation of particulates in the belly portion prior to the flow barrier.
2. The desanding vessel of claim 1 wherein the flow barrier is a downcomer weir.
3. The desanding vessel of claim 1 or 2 wherein the vessel is cylindrical having a substantially horizontal axis.
4. The desanding vessel of claim 1 or 2 wherein the vessel is cylindrical having a substantially horizontal axis extending substantially the length of said vessel wherein the fluid inlet discharges the fluid stream into the freeboard portion of said vessel via an inwardly extending fluid introduction means.
5. The desanding vessel of claim 4 wherein the fluid inlet discharges the fluid stream into the freeboard portion via said fluid introduction means along a fluid path which is substantially parallel to the axis.
6. The desanding vessel of claim 5 wherein the fluid inlet is offset above the axis of said vessel.
7. The desanding vessel of any one of claims 4 - 6 wherein the fluid inlet comprises an eccentric fitting for aligning said fluid introduction means offset from and above said axis, so that fluid is introduced into the vessel above said axis.
8. The desanding vessel of any one of claims 1 - 7 further comprising a cleanout port for periodically accessing and removing said particulates accumulated in the belly portion.
9. The desanding vessel of claim 8 further comprising:
means for de-pressurizing the vessel before opening the cleanout port.
means for de-pressurizing the vessel before opening the cleanout port.
10. A substantially elongate, horizontal vessel for removal of particulates entrained in a fluid stream emanating from a petroleum well, comprising:
a fluid inlet adjacent a first end of the vessel, adapted for receiving the fluid stream and discharging the fluid steam at an inlet velocity into an upper region of said vessel, such vessel having a greater cross-sectional area than said fluid inlet such that said fluid stream entering said vessel slows to a velocity less than said inlet velocity and particulates fall out of suspension and collect on a lower region of said vessel;
a fluid outlet from the vessel, positioned in the upper region of said vessel for directing said fluid stream having particulates substantially removed therefrom from the vessel;
a flow barrier, positioned in a path of flow of said fluid stream from said fluid inlet to said fluid outlet, said flow barrier directing the path of flow of said fluid stream thereunder; and a belly portion for accumulating said particulates prior to said flow barrier.
a fluid inlet adjacent a first end of the vessel, adapted for receiving the fluid stream and discharging the fluid steam at an inlet velocity into an upper region of said vessel, such vessel having a greater cross-sectional area than said fluid inlet such that said fluid stream entering said vessel slows to a velocity less than said inlet velocity and particulates fall out of suspension and collect on a lower region of said vessel;
a fluid outlet from the vessel, positioned in the upper region of said vessel for directing said fluid stream having particulates substantially removed therefrom from the vessel;
a flow barrier, positioned in a path of flow of said fluid stream from said fluid inlet to said fluid outlet, said flow barrier directing the path of flow of said fluid stream thereunder; and a belly portion for accumulating said particulates prior to said flow barrier.
11. The vessel of claim 10 wherein the flow barrier is a downcomer weir for maintaining the upper region of said vessel.
12. The desanding vessel of claim 10 or 11 wherein the vessel is cylindrical having a substantially horizontal axis.
13. The vessel of claim 11 or 12 wherein the vessel is cylindrical having a substantially horizontal axis extending substantially the length of said vessel wherein the fluid inlet discharges the fluid stream into the upper portion of said vessel via an inwardly extending fluid introduction means.
14. The vessel of claim 13 wherein the inlet discharges the fluid stream into the upper portion via said fluid introduction means along a fluid path which is substantially parallel to the axis.
15. The vessel of claim 14 wherein the fluid inlet is offset above the axis of said vessel.
16. The vessel of any one of claims 13 - 15 wherein the fluid inlet comprises an eccentric fitting for aligning said fluid introduction means offset from and above said axis, so that fluid is introduced into the vessel above said axis.
17. The vessel of any one of claims 10 - 16 further comprising a cleanout port for periodically accessing and removing particles accumulated in the belly portion.
18. The vessel of claim 17 further comprising means for de-pressurizing the vessel before opening the cleanout port.
19. A substantially elongate, horizontal vessel for removal of particulates entrained in a fluid stream emanating from a petroleum well, comprising:
an upper region;
a lower belly region;
a fluid inlet adjacent a first end of the vessel, adapted for receiving the fluid stream having an inlet velocity and discharging the fluid stream into said upper region of said vessel, said upper region having a greater cross-sectional area than said fluid inlet such that said fluid stream slows to a velocity less than said inlet velocity and particulates fall out of suspension and collect on said lower belly region of said vessel;
a fluid outlet from the vessel, spaced horizontally from the fluid inlet and situated proximate a second opposite end of said vessel, positioned in said upper region of said vessel; and a flow barrier extending downwardly through said upper region so as to direct the fluid stream below the flow barrier before the fluid stream discharges from the fluid outlet, the flow barrier being positioned between the fluid inlet and fluid outlet and spaced from the fluid inlet to permit accumulation of said particulates in said lower belly region prior to the flow barrier.
an upper region;
a lower belly region;
a fluid inlet adjacent a first end of the vessel, adapted for receiving the fluid stream having an inlet velocity and discharging the fluid stream into said upper region of said vessel, said upper region having a greater cross-sectional area than said fluid inlet such that said fluid stream slows to a velocity less than said inlet velocity and particulates fall out of suspension and collect on said lower belly region of said vessel;
a fluid outlet from the vessel, spaced horizontally from the fluid inlet and situated proximate a second opposite end of said vessel, positioned in said upper region of said vessel; and a flow barrier extending downwardly through said upper region so as to direct the fluid stream below the flow barrier before the fluid stream discharges from the fluid outlet, the flow barrier being positioned between the fluid inlet and fluid outlet and spaced from the fluid inlet to permit accumulation of said particulates in said lower belly region prior to the flow barrier.
20. The vessel of claim 19 wherein the flow barrier is a downcomer weir.
21. The vessel of claim 19 or 20 wherein the vessel is cylindrical having a substantially horizontal axis.
22. The vessel of claims 19 or 20 wherein the vessel is cylindrical having a substantially horizontal axis extending substantially the length of said vessel wherein the fluid inlet discharges the fluid stream into the upper portion of said vessel via an inwardly extending fluid introduction means.
23. The vessel of claim 22 wherein inlet discharges the fluid stream into the upper region via said fluid introduction means along a fluid path which is substantially parallel to the axis.
24. The vessel of claim 23 wherein the fluid inlet is offset above the axis of said vessel.
25. The vessel of any one of claims 22 - 24 wherein the fluid inlet comprises an eccentric fitting for aligning said fluid introduction means offset from and above said axis, so that fluid is introduced into the vessel above said axis.
26. The vessel of any one of claims 20 - 25 further comprising a cleanout port for periodically accessing and removing said particulates accumulated in the belly portion.
27. The vessel of claim 26 further comprising means for de-pressurizing the vessel before opening the cleanout port.
28. A system for removing particulates entrained in a fluid stream emanating from a petroleum well, comprising:
a substantially elongate, horizontal pressure vessel , comprising:
(i) an upper region;
(ii) a lower belly region;
(iii) a fluid inlet situated proximate a first end of said vessel and the upper region thereof, adapted for receiving said fluid stream having an inlet velocity and discharging the fluid stream into said upper region of said vessel, said upper region having a greater cross-sectional area than said fluid inlet such that said fluid stream slows to a velocity less than said inlet velocity and particulates fall out of suspension and collect in said lower belly region of said vessel;
(iv) a fluid outlet from the vessel, situated at a second end of said vessel opposite said first end;
(v) a flow barrier, extending downwardly through said upper region and situated proximate said fluid outlet so as to direct the fluid stream below the flow barrier immediately before the fluid stream travels upwardly and discharges from the fluid outlet, positioned between the fluid inlet and fluid outlet and spaced from the fluid inlet to permit accumulation of said particulates in said lower belly region;
(vi) a clean-out port proximate said second end, to permit access to said vessel to remove particulates collected in said belly region during a cleaning step;
(vii) means for depressurizing said vessel during said cleaning step; and an inlet flow valve, situated proximate said fluid inlet on said pressure vessel; and an outlet flow valve, situated proximate said fluid outlet on said pressure vessel.
a substantially elongate, horizontal pressure vessel , comprising:
(i) an upper region;
(ii) a lower belly region;
(iii) a fluid inlet situated proximate a first end of said vessel and the upper region thereof, adapted for receiving said fluid stream having an inlet velocity and discharging the fluid stream into said upper region of said vessel, said upper region having a greater cross-sectional area than said fluid inlet such that said fluid stream slows to a velocity less than said inlet velocity and particulates fall out of suspension and collect in said lower belly region of said vessel;
(iv) a fluid outlet from the vessel, situated at a second end of said vessel opposite said first end;
(v) a flow barrier, extending downwardly through said upper region and situated proximate said fluid outlet so as to direct the fluid stream below the flow barrier immediately before the fluid stream travels upwardly and discharges from the fluid outlet, positioned between the fluid inlet and fluid outlet and spaced from the fluid inlet to permit accumulation of said particulates in said lower belly region;
(vi) a clean-out port proximate said second end, to permit access to said vessel to remove particulates collected in said belly region during a cleaning step;
(vii) means for depressurizing said vessel during said cleaning step; and an inlet flow valve, situated proximate said fluid inlet on said pressure vessel; and an outlet flow valve, situated proximate said fluid outlet on said pressure vessel.
29. The system for removing particulates as claimed in claim 28, wherein said fluid inlet discharges said fluid stream into said vessel along substantially a horizontal longitudinal axis of said vessel.
30. A method for removing particulates contained in a fluid stream flowing from an existing wellhead, comprising:
receiving the fluid stream at a fluid inlet, the fluid stream being discharged therefrom to a freeboard portion at a top of a vessel, the fluid stream in the freeboard portion having a freeboard velocity less than an inlet velocity of said fluid stream so that said particulates fall out of suspension;
discharging the fluid stream from a fluid outlet spaced horizontally from the fluid inlet; and further comprising the interim step prior to discharging said fluid stream from said fluid outlet of:
directing the fluid stream below a flow barrier depending from the top of the vessel for maintaining the freeboard portion and forming a belly storage portion therebelow, the flow barrier being positioned between the fluid inlet and fluid outlet and the flow barrier being spaced from the fluid inlet; and accumulating the particulates in the belly portion prior to said flow barrier so that fluid stream at the fluid outlet is substantially free of particulates.
receiving the fluid stream at a fluid inlet, the fluid stream being discharged therefrom to a freeboard portion at a top of a vessel, the fluid stream in the freeboard portion having a freeboard velocity less than an inlet velocity of said fluid stream so that said particulates fall out of suspension;
discharging the fluid stream from a fluid outlet spaced horizontally from the fluid inlet; and further comprising the interim step prior to discharging said fluid stream from said fluid outlet of:
directing the fluid stream below a flow barrier depending from the top of the vessel for maintaining the freeboard portion and forming a belly storage portion therebelow, the flow barrier being positioned between the fluid inlet and fluid outlet and the flow barrier being spaced from the fluid inlet; and accumulating the particulates in the belly portion prior to said flow barrier so that fluid stream at the fluid outlet is substantially free of particulates.
31. The method of claim 30 wherein the vessel is cylindrical having a substantially horizontal axis, the method further comprising the step of discharging the fluid stream into the freeboard portion along a fluid path which is substantially parallel to the vessel's axis and offset above the vessel's axis.
32. The method of claim 30 or 31 further comprising periodically accessing the vessel and removing said particulates accumulated in the belly portion.
33. The method of claim 32 further comprising depressurizing the vessel prior to the periodic accessing and removing of said particulates accumulated in the belly portion.
34. The method of claims 30 or 31 further comprising periodically depressurizing the vessel prior to accessing and removing said particulates accumulated in the belly portion prior to the flow barrier.
Priority Applications (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA002526233A CA2526233A1 (en) | 2002-10-10 | 2002-10-10 | Desanding apparatus and system |
| CA002407554A CA2407554C (en) | 2002-10-10 | 2002-10-10 | Method and apparatus for desanding wellhead production |
| CA002535215A CA2535215C (en) | 2002-10-10 | 2002-10-10 | System, method and apparatus for desanding wellhead production |
| CA002433741A CA2433741C (en) | 2002-10-10 | 2003-06-27 | Desanding apparatus and system |
| US10/668,266 US6983852B2 (en) | 2002-10-10 | 2003-09-24 | Desanding apparatus and system |
| US11/164,675 US7383958B2 (en) | 2002-10-10 | 2005-12-01 | Desanding apparatus and system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA002407554A CA2407554C (en) | 2002-10-10 | 2002-10-10 | Method and apparatus for desanding wellhead production |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002535215A Division CA2535215C (en) | 2002-10-10 | 2002-10-10 | System, method and apparatus for desanding wellhead production |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2407554A1 CA2407554A1 (en) | 2004-04-10 |
| CA2407554C true CA2407554C (en) | 2006-06-20 |
Family
ID=32331645
Family Applications (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002407554A Expired - Lifetime CA2407554C (en) | 2002-10-10 | 2002-10-10 | Method and apparatus for desanding wellhead production |
| CA002535215A Expired - Lifetime CA2535215C (en) | 2002-10-10 | 2002-10-10 | System, method and apparatus for desanding wellhead production |
| CA002526233A Pending CA2526233A1 (en) | 2002-10-10 | 2002-10-10 | Desanding apparatus and system |
Family Applications After (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002535215A Expired - Lifetime CA2535215C (en) | 2002-10-10 | 2002-10-10 | System, method and apparatus for desanding wellhead production |
| CA002526233A Pending CA2526233A1 (en) | 2002-10-10 | 2002-10-10 | Desanding apparatus and system |
Country Status (1)
| Country | Link |
|---|---|
| CA (3) | CA2407554C (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9909405B2 (en) | 2012-02-13 | 2018-03-06 | Specialized Desanders Inc. | Desanding apparatus and a method of using same |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101265797B (en) * | 2008-04-30 | 2015-03-25 | 安东石油技术（集团）有限公司 | Flow string possessing water controlling valve and longitudinal rib |
| US8945395B2 (en) | 2011-11-29 | 2015-02-03 | Bonavista Energy Corporation | Settling vessel and method of use |
| US9327214B2 (en) | 2012-02-13 | 2016-05-03 | Specialized Desanders Inc. | Desanding apparatus and a method of using same |
| US9938812B2 (en) | 2012-02-13 | 2018-04-10 | Specialized Desanders Inc. | Desanding apparatus and a method of using same |
| CN104060978B (en) * | 2013-06-28 | 2017-06-23 | 中国石油天然气股份有限公司 | Multi-cylinder cyclone desander and desanding method |
| CA2836437A1 (en) | 2013-12-16 | 2015-06-16 | Specialized Desanders Inc. | An desanding apparatus and a method of using the same |
| BR112017011614A2 (en) | 2014-12-04 | 2018-03-06 | Specialized Desanders Inc. | drainage apparatus and method of use |
| CN107060722A (en) * | 2016-10-26 | 2017-08-18 | 胜利油田瑞特石油机械制造有限责任公司 | High pressure cyclone filtering type natural gas desander |
| AU2018276084B2 (en) | 2017-05-30 | 2023-05-04 | Specialized Desanders Inc. | Gravity desanding apparatus with filter polisher |
| US10967305B2 (en) | 2017-05-30 | 2021-04-06 | Specialized Desanders Inc. | Boundary layer modification in closely-spaced passages |
-
2002
- 2002-10-10 CA CA002407554A patent/CA2407554C/en not_active Expired - Lifetime
- 2002-10-10 CA CA002535215A patent/CA2535215C/en not_active Expired - Lifetime
- 2002-10-10 CA CA002526233A patent/CA2526233A1/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9909405B2 (en) | 2012-02-13 | 2018-03-06 | Specialized Desanders Inc. | Desanding apparatus and a method of using same |
Also Published As
| Publication number | Publication date |
|---|---|
| CA2535215A1 (en) | 2004-04-10 |
| CA2526233A1 (en) | 2004-04-10 |
| CA2535215C (en) | 2007-05-08 |
| CA2407554A1 (en) | 2004-04-10 |
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| EEER | Examination request | ||
| MKEX | Expiry |
Effective date: 20221011 |