CA2041979A1 - Steam distribution manifold - Google Patents
Steam distribution manifoldInfo
- Publication number
- CA2041979A1 CA2041979A1 CA002041979A CA2041979A CA2041979A1 CA 2041979 A1 CA2041979 A1 CA 2041979A1 CA 002041979 A CA002041979 A CA 002041979A CA 2041979 A CA2041979 A CA 2041979A CA 2041979 A1 CA2041979 A1 CA 2041979A1
- Authority
- CA
- Canada
- Prior art keywords
- manifold
- flow disperser
- vapor
- outlet ports
- liquid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21B—EARTH DRILLING, e.g. DEEP 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
- E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
- E21B43/24—Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21B—EARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B36/00—Heating, cooling, insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/0318—Processes
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/8593—Systems
- Y10T137/85938—Non-valved flow dividers
Abstract
STEAM DISTRIBUTION MANIFOLD
ABSTRACT OF THE DISCLOSURE
A manifold for dividing a single, two-phase mixed stream of vapor and liquid into a plurality of individual streams of substantially uniform quality. The manifold comprises: a flow disperser having an inlet port for receiving the vapor-liquid mixture and at least two outlet ports; at least two hollow runners, each runner having a first end in fluid communication with one of the outlet ports of the flow disperser and a second end; a substantially toroidal manifold shell having at least two fluid receiver ports in fluid communication with each of the second ends of the runners, the manifold shell defining a manifold chamber; and a plurality of distribution ports spaced about the substantially toroidal manifold shell, each distribution port in fluid communication with the manifold chamber of the toroidal manifold shell; wherein the vapor-liquid mixture emanating from each distribution port of the manifold is of substantially uniform quality. A method for uniformly distributing a vapor-liquid mixture is also provided.
ABSTRACT OF THE DISCLOSURE
A manifold for dividing a single, two-phase mixed stream of vapor and liquid into a plurality of individual streams of substantially uniform quality. The manifold comprises: a flow disperser having an inlet port for receiving the vapor-liquid mixture and at least two outlet ports; at least two hollow runners, each runner having a first end in fluid communication with one of the outlet ports of the flow disperser and a second end; a substantially toroidal manifold shell having at least two fluid receiver ports in fluid communication with each of the second ends of the runners, the manifold shell defining a manifold chamber; and a plurality of distribution ports spaced about the substantially toroidal manifold shell, each distribution port in fluid communication with the manifold chamber of the toroidal manifold shell; wherein the vapor-liquid mixture emanating from each distribution port of the manifold is of substantially uniform quality. A method for uniformly distributing a vapor-liquid mixture is also provided.
Description
20~979 F-~718 STEAM DISTRIBUTION MANIFOLD
Field of the Invention The present invention relates to an apparatus and method for dividing a single, ~wo-phase mixed stream of vapor anc liquid into a plurality of individual uniform quality streams.
More particularly, the present invention employs a manifold of toroidal configuration which receives a single two-phase mixed stream from a supply line and divides it into a plurality of streams for distribution therefrom.
Backaround o~ the Invention There are many oil~bearing sub~erranean formations fron which the resident oil cannot be recovered in economic quantitieC
by primary recovery techniques. In these formations, secondary recovery techniques must be employed to enable the oil to ~e produced in economic quantities. One of the secondary recovery techniques which has been found to be well-suited for use in these formations is known generally as steam stimulation. In this technique, steam is injected into the formation for a perioa of time until the formation is heated sufficiently well so that the viscosity of the oil contained therein is reduced to a degree that it may be readily produced.
Fundamentallyl water can exist as either a gas or a liquid under saturated conditions. Wet steam can contain both gas and liquid components, known to those skilled in the art as two-phase flow. A common method of expressing the quantities of each phase, known as quality, is the ratio of the mass flow rate of the gas phase to the total mass flow rate, expressed as a 7 ~
number less than one or as a percentage. Another expression of steam quality is the use of the ratio of vapor to liquid.
In thermally enhanced oil recovery projects it is common to employ a high quality, two-phase steam which may be prepared for convenience at a central steam generating facility.
As is well known to those skilled in the art, the practice of utilizing a high quality, two-phase steam is necessitated by the use of low quality, brackish wa~ers having at least a moderate level of dissolved solids. To prevent deposition of salts on th surface of the steam generator tubes, it is necessary to retain part of the flow in a liquid state in order to maintain the solids and other impuri~ies in solution. As can be appreciated, should the steam so generated be required to be distributed to a plurality of injection wells from a single generator output line it is esæential that this plurality of individual ~lows be maintained at a consistent and desirable vapor-to-liquid ratio.
The problem which exists in the distribution of a two-phase mixe stream of vapor and liquid to a plurality of locations is that without special provisions, the vapor and liquid components will not divide into flows of uniform vapor-to-liquid ratio.
Several attempts have been made to provide an apparatuc for distributing a two-phase mixed stream of vapor and liquid.
For example, U. S. Patent No. 3,899,000 provides a closed vessel structure for the separation of a two-phase vapor-liquid mixture into two or more individual flows. The vessel disclosed is mountad vertically and proYided with a top inlet and two or more bottom outlets. A flat, horizontal baffle is used to divert the inlet flow from the open ends of the outlets. The axis of the inlet and the axis of the outlets are substantially parallel so that the flow of the fluid is axially through the elongated vessel. It is tauyht ~hat the vapor-to-liquid ratio is maintained by using the outlets as standpipes and the vessel as a 2 ~
reservoir. Once sufficiant liquid collects in the bo~tom of th~
vessel, it can overflow the side outlets in the standpipes and liquid will be added to the vapor flowing out of the outlets.
U. S. Patent No. 4,269,211 discloses a method for equalizing the steam quality in a plurality of branch lines of a high pressure steam pipeline. Also disclosed is a steam manifolc distribution system which includes a mechanism for retracting a perforated baffle plate into a pressure equalizer chamber for removal, repair or replacement of the baffle plate. The pressur~
equalizer chamber of U. S. Patent No. 4,269,211 may be positionec on and fixedly attached to a tee joint in the the field in any position between and coaxial with one of the branch lines of the tee joint and perpendicular thereto.
U. S. Patent No. 4,505,297 discloses an apparatus for dividing a single stream vapor-liquid mixture into a plurality ol individual streams while maintaining a similar vapor-to-liquid ratio in the individual streams. The apparatus taught comprises a closed vessel having a central inlet in the top for the inlet feedstream and a plurality of outlets in the side of the vessel for the individual streams. A frustrum-shaped diverting member is mounted in the center of the vessel to divert the flow of the single feedstream into the individual streams. A bottom drain ic disclosed for use in removing any liquid that is separated from the vapor-liquid mixture.
U. S. Patent No. 4,800,921 teachas the utilization of a gravity influenced liquid distribution system in an annular flow regime within a substantially horizontal header which receives a liquid vapor mixture from a supply line and divides that single stream into a plurality of streams for distribution through a branch}ine to a nearby site. The header employed is substantially horizontal, with each branchline connected to the 2~197~
periphery of the header further downstream and relatively lower on the periphery of the header than the pre~eding branchline.
Despite these advances in the art, there exists a need for an improved steam manifold and distribution system capable o:
uniformly distributing steam throughout a field through a plurality of steam distribution lines.
Summary of the_Invention According to the present invention, there is provided .
manifold for dividing a single, two-phase mixed stream of vapor and liquid into a plurality of individual streams of substantially uniform quality. The manifold comprises: a flow disperser having an inlet port for receiving the vapor-liquid mixture and at least two outlet ports; at least two hollow runners, each runner having a first end in fluid communication with one of the outlet ports of the flow disperser and a second end; a substantially toroidal manifold shell haYing at least two fluid receiver ports in fluid communication with each of the second ends of the runners, the manifold shell defining a manifold chamber; and a plurality of distribution ports spaced about the substantially toroidal manifold shell, each distrihution port in fluid communication with the manifold chamber of the toroidal manifold shell; wherein the vapor-liquid mixture emanating from each distribution port of the manifold is of substantially uniform quality.
A method for dividing a two-phase mixed stream of vapor and liquid into a plurality o~ individual streams of substantially uniform quality i5 also provided. The method comprises the steps of: feeding a two-phase mixed str~am of vapor and liquid at a first velocity into a generally toroidally configured steam distribution manifold along a first axis;
diverting the two-phase mixed stream of vapor and liquid along a 2~1979 second axis; increasing the velocity of the diverted two-phase mixed s ream to a second v010city: and dividing the two-phase mixed stream of vapor and liquid into a plurality o~ individual streams of substantially uni~orm quality.
Therefore, it is an object of the present invention to provide a manifold for dividing a single, two-phase mixed stream of vapor and liquid into a plurality of individual streams havinc substantially uniform vapor-to-liquid ratios.
Another object of the present invention resides in the provision of a manifold for distributing uniform quality wet steam from a single trunk line ~o multiple steam injector sites which is capable of effective use in an oil ~ield environment.
Yet another object of the present invention is to provide a manifold for dividing a single vapor-liquid mixture stream into a plurality of individual streams of substantially uniform quality which is of simple configuration and easy to fabricate.
Still another object of the present invention is the provision of a manifold for distributing uniform quality wet steam from a single trunk line to multiple staam injector sites which is easy to operate and requires little maintenance.
It is a further object of the present invention to provide a method for uniformly dividlng a single vapor-liquid mixture stream into a plurality of individual streams of substantially uniform quality.
Other objects and the several advantages of tha present invention will become apparent to those skilled in the art upon a reading of the specification and the claims appended thereto.
Brie~ DescrlptIon of the Drawin~s Fig. 1 is a side elevational view of a steam distribution manifold in accordanca with the present invention.
9 ~ 9 Fig. 2 is a top plan view of the steam distribution mani~old o~ Figure 1.
Fig. 3 is an enlarged ~ragmen'cary sectional view taken along the lin~ A-A of Fig. 2.
Detailed Description of the Present Invention The present invention is best understood by reference to ~he appended ~igures, which are given by way of example and not of limitation. Referring now to Fig. 1, a side elevational view o~ steam distribution manifold 1, is shown. In opPration, wet steam is fed through trunk line 28 to centrally located steam inlet port 4 of steam distribution manifold 1 where it travels to flow disperser 2 for horizontal diversion to toroidal manifold shell 10. As can be envisioned by reference to Fig. 3, the interior sur~ace of toroidal manifold shell 10 defines manifold chamber 14. The vapor-liquid mixture is drawn from manifold chamber 14 in response to various field injector requirements through a plurality of distribution ports 16. ~s is preferred, distribution ports 16 can be advanta~eously located on the upper peripheral surface of toroidal manifold shell 10. The vapor-liquid mixture then passes through distribution legs 18 to individual injection wells (not shown). It is preferred that distribution ports 16 each have the same diameter, with the flow from each leg 18 to the individual wells controlled by metering valves 22.
Optionally, steam distribution manifold 1 can employ a static mixer 24, preferably located directly below steam inlet port 4. Such a mixer, as those skilled in the art recognize, is designed to thoroughly distribute the liquid o~ the vapor-liquid mixture throughout the fluid. An example of such a mixer is the Komax~ Triple Action Motionles~ Mixer, marketed by Komax Systems, Inc. o~ Long Beach, CA.
20~1 979 Referring now to Fig. 2, a top plan viaw of steam distribution mani~old 1 is presented. As can be seen, flow disperser 2 diverts the vapor-liquid feedstream horizontally through outlet ports 6 to hollow runners 8 which are in fluid communication with fluid receiver ports 12 of toxoidal manifold shell 10. To achieve uniform flow and distribution o~ the vapor-liquid mixture, it is pre~erred that at least two runners be employed to feed the vapor-liquid stream into manifold chambe~
14 of toroidal manifold shell 10: with four runners 8, spaced uniformly a~out toroidal manifold shell 10, as is shown, still more preferred. It is also preferred that distribution ports 16 be spaced uniformly about the sectors of the toroidal manifold shell 10. The term sec~or ref~rs to that portion of the toroidal manifold shell 10 defined by radial lines through any two ad~acent fluid receiver ports 12. As can be appreciated by thos~
skilled in the art, it is advantageous not to locate a distribution port 16 directly adjacent a fluid receiver port 2 and, for this reason, the mani~old depicted in Fig. 2 does not employ uni~orm distribution port 16 spacing about the circumference of toroidal manifold shell 10; but rather employs uniform spacing within each sector, as preferred.
Referring now to Fig. 3, an enlarged fragmentary section taken along the line A-A o~ Fig. 2 is shown. As can be envisioned, wet steam, mixed and channeled, will flow up to steam inlet port 4 where it then travels to ~low disperser 2 for horizontal diversion to outlet por~s 6 and runners 8. Shown within flow disperser 2 is diverting member 20. Diverting member 20 sQrves to divide the flow evenly among the runners 8 without inducing excessive amo-lnts of turbulence to the flow stream. As is preferred, diverting member 20 can be a substantially conical structure, although structures having other configurations may have utility in this application. As can be appreciated, a 7 ~
diverting member of generally frustrum shape could be fabricated form sheet metal stock to have ~lat sides, for example three or more. To enable runners 8 to exhibit substantially equal pressure drops across their respective lengths, it was found that the flow rate of the vapor~ uid mixture through each runner 8 must exceed that found within the manifold chamber 14 of toroidal manifold shell lO. To achieve this phenomena, it was found necessary to obtain a Reynolds number 20% higher than tha~ of trunk line 28 (see Fig. 1). The high resulting pressure drop allows fox the uniform flow of the vapor-liquid mixture about manifold chamber 14 of toroidal manifold shell 10, even at the points where the mixture is being withdrawn from manifold l for downstream field use. The increased velocity also insures that the mixture travels about manifold cham~er 14 of toroidal manifold shell 10 in a mist flow pattern, a pattern most ideal for maintaining even quality within manifold 1.
Reference is again made to Fig. z. By providing toroidal manifold shell lO with a relative}y tight radius L
excellent mixing of the vapor-liquid fluid is achieved. The degree of turbulence provided aids in the prevention o~ flow conditions which could cause separation or stratification of the vapor-liquid mixture. Such a configuration also improves the flow response to changes in steam injector line feed demands.
The invention is further by the following non-limiting example.
EXAMPLE
A steam distribution manifold was built in accordance with the present invention, substantially as shown in the appended Figures 1-3. The manifold was designed to distri~ute uniform quality wet steam to 16 steam injector lines employed in a particular oil field from a 4" diameter steam trunk line.
2 ~ 7 9 Toroidal manifold shell lo was fabricated from 6" diameter steel tubing and provided with a radius L of approximately 2~. Flow disperser 2 was constructed ~rom a 4" schedule 80 cross and fitted with a substantially conical diverting member 20. Four 4 x 2" concentric reducers were installed on flow disperser 2, to serve as outlet ports 6. Runners 8 were ~abricated using 2"
diameter schedule 160 pipe. Such dimensianing provided the requisite pressure drop to achieve uniform flow. Fluid receiver ports 12 were constructed using 6" x 2" concentric reducers. Al 16 steam injector lines had diameters of 3". The manifold was installed and found to uniformly distribute the vapor-liquid wet steam mixture, with minimal variance in vapor-to-liquid ratio observed.
Although the present in~ention has been described with preferred em~odiments, it is to be understood that modifications and variations may be utilized without departing from the spirit and scope of this invention, as those skilled in the art will readily understand. Such modifications and variations are considered to be within the purYiew and scope o~ the appended claims.
Field of the Invention The present invention relates to an apparatus and method for dividing a single, ~wo-phase mixed stream of vapor anc liquid into a plurality of individual uniform quality streams.
More particularly, the present invention employs a manifold of toroidal configuration which receives a single two-phase mixed stream from a supply line and divides it into a plurality of streams for distribution therefrom.
Backaround o~ the Invention There are many oil~bearing sub~erranean formations fron which the resident oil cannot be recovered in economic quantitieC
by primary recovery techniques. In these formations, secondary recovery techniques must be employed to enable the oil to ~e produced in economic quantities. One of the secondary recovery techniques which has been found to be well-suited for use in these formations is known generally as steam stimulation. In this technique, steam is injected into the formation for a perioa of time until the formation is heated sufficiently well so that the viscosity of the oil contained therein is reduced to a degree that it may be readily produced.
Fundamentallyl water can exist as either a gas or a liquid under saturated conditions. Wet steam can contain both gas and liquid components, known to those skilled in the art as two-phase flow. A common method of expressing the quantities of each phase, known as quality, is the ratio of the mass flow rate of the gas phase to the total mass flow rate, expressed as a 7 ~
number less than one or as a percentage. Another expression of steam quality is the use of the ratio of vapor to liquid.
In thermally enhanced oil recovery projects it is common to employ a high quality, two-phase steam which may be prepared for convenience at a central steam generating facility.
As is well known to those skilled in the art, the practice of utilizing a high quality, two-phase steam is necessitated by the use of low quality, brackish wa~ers having at least a moderate level of dissolved solids. To prevent deposition of salts on th surface of the steam generator tubes, it is necessary to retain part of the flow in a liquid state in order to maintain the solids and other impuri~ies in solution. As can be appreciated, should the steam so generated be required to be distributed to a plurality of injection wells from a single generator output line it is esæential that this plurality of individual ~lows be maintained at a consistent and desirable vapor-to-liquid ratio.
The problem which exists in the distribution of a two-phase mixe stream of vapor and liquid to a plurality of locations is that without special provisions, the vapor and liquid components will not divide into flows of uniform vapor-to-liquid ratio.
Several attempts have been made to provide an apparatuc for distributing a two-phase mixed stream of vapor and liquid.
For example, U. S. Patent No. 3,899,000 provides a closed vessel structure for the separation of a two-phase vapor-liquid mixture into two or more individual flows. The vessel disclosed is mountad vertically and proYided with a top inlet and two or more bottom outlets. A flat, horizontal baffle is used to divert the inlet flow from the open ends of the outlets. The axis of the inlet and the axis of the outlets are substantially parallel so that the flow of the fluid is axially through the elongated vessel. It is tauyht ~hat the vapor-to-liquid ratio is maintained by using the outlets as standpipes and the vessel as a 2 ~
reservoir. Once sufficiant liquid collects in the bo~tom of th~
vessel, it can overflow the side outlets in the standpipes and liquid will be added to the vapor flowing out of the outlets.
U. S. Patent No. 4,269,211 discloses a method for equalizing the steam quality in a plurality of branch lines of a high pressure steam pipeline. Also disclosed is a steam manifolc distribution system which includes a mechanism for retracting a perforated baffle plate into a pressure equalizer chamber for removal, repair or replacement of the baffle plate. The pressur~
equalizer chamber of U. S. Patent No. 4,269,211 may be positionec on and fixedly attached to a tee joint in the the field in any position between and coaxial with one of the branch lines of the tee joint and perpendicular thereto.
U. S. Patent No. 4,505,297 discloses an apparatus for dividing a single stream vapor-liquid mixture into a plurality ol individual streams while maintaining a similar vapor-to-liquid ratio in the individual streams. The apparatus taught comprises a closed vessel having a central inlet in the top for the inlet feedstream and a plurality of outlets in the side of the vessel for the individual streams. A frustrum-shaped diverting member is mounted in the center of the vessel to divert the flow of the single feedstream into the individual streams. A bottom drain ic disclosed for use in removing any liquid that is separated from the vapor-liquid mixture.
U. S. Patent No. 4,800,921 teachas the utilization of a gravity influenced liquid distribution system in an annular flow regime within a substantially horizontal header which receives a liquid vapor mixture from a supply line and divides that single stream into a plurality of streams for distribution through a branch}ine to a nearby site. The header employed is substantially horizontal, with each branchline connected to the 2~197~
periphery of the header further downstream and relatively lower on the periphery of the header than the pre~eding branchline.
Despite these advances in the art, there exists a need for an improved steam manifold and distribution system capable o:
uniformly distributing steam throughout a field through a plurality of steam distribution lines.
Summary of the_Invention According to the present invention, there is provided .
manifold for dividing a single, two-phase mixed stream of vapor and liquid into a plurality of individual streams of substantially uniform quality. The manifold comprises: a flow disperser having an inlet port for receiving the vapor-liquid mixture and at least two outlet ports; at least two hollow runners, each runner having a first end in fluid communication with one of the outlet ports of the flow disperser and a second end; a substantially toroidal manifold shell haYing at least two fluid receiver ports in fluid communication with each of the second ends of the runners, the manifold shell defining a manifold chamber; and a plurality of distribution ports spaced about the substantially toroidal manifold shell, each distrihution port in fluid communication with the manifold chamber of the toroidal manifold shell; wherein the vapor-liquid mixture emanating from each distribution port of the manifold is of substantially uniform quality.
A method for dividing a two-phase mixed stream of vapor and liquid into a plurality o~ individual streams of substantially uniform quality i5 also provided. The method comprises the steps of: feeding a two-phase mixed str~am of vapor and liquid at a first velocity into a generally toroidally configured steam distribution manifold along a first axis;
diverting the two-phase mixed stream of vapor and liquid along a 2~1979 second axis; increasing the velocity of the diverted two-phase mixed s ream to a second v010city: and dividing the two-phase mixed stream of vapor and liquid into a plurality o~ individual streams of substantially uni~orm quality.
Therefore, it is an object of the present invention to provide a manifold for dividing a single, two-phase mixed stream of vapor and liquid into a plurality of individual streams havinc substantially uniform vapor-to-liquid ratios.
Another object of the present invention resides in the provision of a manifold for distributing uniform quality wet steam from a single trunk line ~o multiple steam injector sites which is capable of effective use in an oil ~ield environment.
Yet another object of the present invention is to provide a manifold for dividing a single vapor-liquid mixture stream into a plurality of individual streams of substantially uniform quality which is of simple configuration and easy to fabricate.
Still another object of the present invention is the provision of a manifold for distributing uniform quality wet steam from a single trunk line to multiple staam injector sites which is easy to operate and requires little maintenance.
It is a further object of the present invention to provide a method for uniformly dividlng a single vapor-liquid mixture stream into a plurality of individual streams of substantially uniform quality.
Other objects and the several advantages of tha present invention will become apparent to those skilled in the art upon a reading of the specification and the claims appended thereto.
Brie~ DescrlptIon of the Drawin~s Fig. 1 is a side elevational view of a steam distribution manifold in accordanca with the present invention.
9 ~ 9 Fig. 2 is a top plan view of the steam distribution mani~old o~ Figure 1.
Fig. 3 is an enlarged ~ragmen'cary sectional view taken along the lin~ A-A of Fig. 2.
Detailed Description of the Present Invention The present invention is best understood by reference to ~he appended ~igures, which are given by way of example and not of limitation. Referring now to Fig. 1, a side elevational view o~ steam distribution manifold 1, is shown. In opPration, wet steam is fed through trunk line 28 to centrally located steam inlet port 4 of steam distribution manifold 1 where it travels to flow disperser 2 for horizontal diversion to toroidal manifold shell 10. As can be envisioned by reference to Fig. 3, the interior sur~ace of toroidal manifold shell 10 defines manifold chamber 14. The vapor-liquid mixture is drawn from manifold chamber 14 in response to various field injector requirements through a plurality of distribution ports 16. ~s is preferred, distribution ports 16 can be advanta~eously located on the upper peripheral surface of toroidal manifold shell 10. The vapor-liquid mixture then passes through distribution legs 18 to individual injection wells (not shown). It is preferred that distribution ports 16 each have the same diameter, with the flow from each leg 18 to the individual wells controlled by metering valves 22.
Optionally, steam distribution manifold 1 can employ a static mixer 24, preferably located directly below steam inlet port 4. Such a mixer, as those skilled in the art recognize, is designed to thoroughly distribute the liquid o~ the vapor-liquid mixture throughout the fluid. An example of such a mixer is the Komax~ Triple Action Motionles~ Mixer, marketed by Komax Systems, Inc. o~ Long Beach, CA.
20~1 979 Referring now to Fig. 2, a top plan viaw of steam distribution mani~old 1 is presented. As can be seen, flow disperser 2 diverts the vapor-liquid feedstream horizontally through outlet ports 6 to hollow runners 8 which are in fluid communication with fluid receiver ports 12 of toxoidal manifold shell 10. To achieve uniform flow and distribution o~ the vapor-liquid mixture, it is pre~erred that at least two runners be employed to feed the vapor-liquid stream into manifold chambe~
14 of toroidal manifold shell 10: with four runners 8, spaced uniformly a~out toroidal manifold shell 10, as is shown, still more preferred. It is also preferred that distribution ports 16 be spaced uniformly about the sectors of the toroidal manifold shell 10. The term sec~or ref~rs to that portion of the toroidal manifold shell 10 defined by radial lines through any two ad~acent fluid receiver ports 12. As can be appreciated by thos~
skilled in the art, it is advantageous not to locate a distribution port 16 directly adjacent a fluid receiver port 2 and, for this reason, the mani~old depicted in Fig. 2 does not employ uni~orm distribution port 16 spacing about the circumference of toroidal manifold shell 10; but rather employs uniform spacing within each sector, as preferred.
Referring now to Fig. 3, an enlarged fragmentary section taken along the line A-A o~ Fig. 2 is shown. As can be envisioned, wet steam, mixed and channeled, will flow up to steam inlet port 4 where it then travels to ~low disperser 2 for horizontal diversion to outlet por~s 6 and runners 8. Shown within flow disperser 2 is diverting member 20. Diverting member 20 sQrves to divide the flow evenly among the runners 8 without inducing excessive amo-lnts of turbulence to the flow stream. As is preferred, diverting member 20 can be a substantially conical structure, although structures having other configurations may have utility in this application. As can be appreciated, a 7 ~
diverting member of generally frustrum shape could be fabricated form sheet metal stock to have ~lat sides, for example three or more. To enable runners 8 to exhibit substantially equal pressure drops across their respective lengths, it was found that the flow rate of the vapor~ uid mixture through each runner 8 must exceed that found within the manifold chamber 14 of toroidal manifold shell lO. To achieve this phenomena, it was found necessary to obtain a Reynolds number 20% higher than tha~ of trunk line 28 (see Fig. 1). The high resulting pressure drop allows fox the uniform flow of the vapor-liquid mixture about manifold chamber 14 of toroidal manifold shell 10, even at the points where the mixture is being withdrawn from manifold l for downstream field use. The increased velocity also insures that the mixture travels about manifold cham~er 14 of toroidal manifold shell 10 in a mist flow pattern, a pattern most ideal for maintaining even quality within manifold 1.
Reference is again made to Fig. z. By providing toroidal manifold shell lO with a relative}y tight radius L
excellent mixing of the vapor-liquid fluid is achieved. The degree of turbulence provided aids in the prevention o~ flow conditions which could cause separation or stratification of the vapor-liquid mixture. Such a configuration also improves the flow response to changes in steam injector line feed demands.
The invention is further by the following non-limiting example.
EXAMPLE
A steam distribution manifold was built in accordance with the present invention, substantially as shown in the appended Figures 1-3. The manifold was designed to distri~ute uniform quality wet steam to 16 steam injector lines employed in a particular oil field from a 4" diameter steam trunk line.
2 ~ 7 9 Toroidal manifold shell lo was fabricated from 6" diameter steel tubing and provided with a radius L of approximately 2~. Flow disperser 2 was constructed ~rom a 4" schedule 80 cross and fitted with a substantially conical diverting member 20. Four 4 x 2" concentric reducers were installed on flow disperser 2, to serve as outlet ports 6. Runners 8 were ~abricated using 2"
diameter schedule 160 pipe. Such dimensianing provided the requisite pressure drop to achieve uniform flow. Fluid receiver ports 12 were constructed using 6" x 2" concentric reducers. Al 16 steam injector lines had diameters of 3". The manifold was installed and found to uniformly distribute the vapor-liquid wet steam mixture, with minimal variance in vapor-to-liquid ratio observed.
Although the present in~ention has been described with preferred em~odiments, it is to be understood that modifications and variations may be utilized without departing from the spirit and scope of this invention, as those skilled in the art will readily understand. Such modifications and variations are considered to be within the purYiew and scope o~ the appended claims.
Claims (20)
1. A manifold for dividing a single, two-phase mixed stream of vapor and liquid into a plurality of individual streams of substantially uniform quality, comprising:
(a) a flow disperser having an inlet port for receiving the vapor-liquid mixture and at least two outlet ports;
(b) at least two hollow runners, each runner having a first end in fluid communication with one of said outlet ports of said flow disperser and a second end;
(c) a substantially toroidal manifold shell having at least two fluid receiver ports in fluid communication with each of said second ends of said runners, said manifold shell defining a manifold chamber: and (d) a plurality of distribution ports spaced about said substantially toroidal manifold shell, each distribution port in fluid communication with said manifold chamber of said toroidal manifold shell;
wherein the vapor-liquid mixture emanating from each said distribution port of the manifold is of substantially uniform quality.
(a) a flow disperser having an inlet port for receiving the vapor-liquid mixture and at least two outlet ports;
(b) at least two hollow runners, each runner having a first end in fluid communication with one of said outlet ports of said flow disperser and a second end;
(c) a substantially toroidal manifold shell having at least two fluid receiver ports in fluid communication with each of said second ends of said runners, said manifold shell defining a manifold chamber: and (d) a plurality of distribution ports spaced about said substantially toroidal manifold shell, each distribution port in fluid communication with said manifold chamber of said toroidal manifold shell;
wherein the vapor-liquid mixture emanating from each said distribution port of the manifold is of substantially uniform quality.
2. The manifold of claim 1, wherein said flow disperser further includes a substantially conical diverting member.
3. The manifold of claim 2, wherein said diverting member is axially aligned with said inlet port of said flow disperser.
4. The manifold of claim 3, wherein said flow disperser includes at least four outlet ports.
5. The manifold of claim 2, wherein said flow disperser includes at least four outlet ports.
6. The manifold of claim 1, wherein said flow disperser includes at least four outlet ports.
7. The manifold of claim 6, wherein said outlet ports of said flow disperser are perpendicularly aligned with said inlet port of said flow disperser.
8. The manifold of claim 1, wherein said outlet ports of said flow disperser are perpendicularly aligned with said inlet port of said flow disperser.
9. The manifold of claim 1, further comprising a static mixer located below said inlet port of said flow disperser.
10. A method for dividing a two-phase mixed stream of vapor and liquid into a plurality of individual streams of substantially uniform quality, comprising the steps of:
(a) feeding a two-phase mixed stream of vapor and liquid at a first velocity into a generally toroidally configured steam distribution manifold along a first axis;
(b) diverting the two-phase mixed stream of vapor and liquid along a second axis;
(c) increasing the velocity of the diverted two-phase mixed stream to a second velocity; and (d) dividing the two-phase mixed stream of vapor and liquid into a plurality of individual streams of substantially uniform quality.
(a) feeding a two-phase mixed stream of vapor and liquid at a first velocity into a generally toroidally configured steam distribution manifold along a first axis;
(b) diverting the two-phase mixed stream of vapor and liquid along a second axis;
(c) increasing the velocity of the diverted two-phase mixed stream to a second velocity; and (d) dividing the two-phase mixed stream of vapor and liquid into a plurality of individual streams of substantially uniform quality.
11. The method of claim 10 wherein the steam distribution manifold comprises:
(a) a flow disperser having an inlet port for receiving the vapor-liquid mixture and at least two outlet ports;
(b) at least two hollow runners, each runner having a first end in fluid communication with one of the outlet ports of the flow disperser and a second end:
(c) a substantially toroidal manifold shell having at least two fluid receiver ports in fluid communication with each of the second ends of the runners, the manifold shell defining a manifold chamber; and (d) a plurality of distribution ports spaced about the substantially toroidal manifold shell, each distribution port in fluid communication with the manifold chamber of the toroidal manifold shell;
(a) a flow disperser having an inlet port for receiving the vapor-liquid mixture and at least two outlet ports;
(b) at least two hollow runners, each runner having a first end in fluid communication with one of the outlet ports of the flow disperser and a second end:
(c) a substantially toroidal manifold shell having at least two fluid receiver ports in fluid communication with each of the second ends of the runners, the manifold shell defining a manifold chamber; and (d) a plurality of distribution ports spaced about the substantially toroidal manifold shell, each distribution port in fluid communication with the manifold chamber of the toroidal manifold shell;
12. The method of claim 11, wherein the flow disperser further includes a substantially conical diverting member.
13. The method of claim 12, wherein the diverting member axially aligned with the inlet port of the flow disperser
14. The method of claim 13, wherein the flow disperser includes at least four outlet ports.
15. The method of claim 12, wherein the flow disperser includes at least four outlet ports.
16. The method of claim 11, wherein the flow disperser includes at least four outlet ports.
17. The method of claim 16, wherein the outlet ports o the flow disperser are perpendicularly aligned with the inlet port of the flow disperser.
18. The method of claim 11, wherein the outlet ports o the flow disperser are perpendicularly aligned with the inlet port of the flow disperser.
19. The method of claim 18, wherein the second axis is perpendicular to the first axis.
20. The method of claim 10, wherein the second axis is perpendicular to the first axis.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/526,475 US5010910A (en) | 1990-05-21 | 1990-05-21 | Steam distribution manifold |
| US526,475 | 1990-05-21 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2041979A1 true CA2041979A1 (en) | 1991-11-22 |
Family
ID=24097509
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002041979A Abandoned CA2041979A1 (en) | 1990-05-21 | 1991-05-07 | Steam distribution manifold |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US5010910A (en) |
| CA (1) | CA2041979A1 (en) |
Families Citing this family (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5709468A (en) * | 1992-11-27 | 1998-01-20 | Texaco Group, Inc. | Method for equalizing steam quality in pipe networks |
| DE4409234A1 (en) * | 1994-03-18 | 1995-09-21 | Zimmer Ag | Distributor for viscous liquids with multiple radial outlets |
| US5810032A (en) * | 1995-03-22 | 1998-09-22 | Chevron U.S.A. Inc. | Method and apparatus for controlling the distribution of two-phase fluids flowing through impacting pipe tees |
| US5710717A (en) * | 1995-03-22 | 1998-01-20 | Chevron U.S.A. Inc. | Method for predicting and adjusting the distribution of two-phase fluids flowing through a piping network |
| AT402826B (en) * | 1995-07-26 | 1997-09-25 | Chemiefaser Lenzing Ag | METHOD FOR TRANSPORTING THERMALLY UNSTABLE, VISCOSIC MASS |
| CA2471349C (en) | 2001-12-21 | 2011-08-23 | Amalgamated Research, Inc. | Toroidal vessel for uniform, plug-flow fluid distribution applications |
| EA005545B1 (en) * | 2002-01-03 | 2005-04-28 | Пакс Сайентифик, Инк. | Vortex ring generator |
| AUPR982302A0 (en) * | 2002-01-03 | 2002-01-31 | Pax Fluid Systems Inc. | A fluid flow controller |
| AUPR982502A0 (en) * | 2002-01-03 | 2002-01-31 | Pax Fluid Systems Inc. | A heat exchanger |
| AU2003903386A0 (en) | 2003-07-02 | 2003-07-17 | Pax Scientific, Inc | Fluid flow control device |
| KR101168098B1 (en) * | 2003-11-04 | 2012-07-24 | 팍스 싸이언티픽 인코퍼레이션 | Fluid Circulation System |
| WO2005073561A1 (en) * | 2004-01-30 | 2005-08-11 | Pax Scientific, Inc | Housing for a centrifugal fan, pump or turbine |
| WO2005073560A1 (en) * | 2004-01-30 | 2005-08-11 | Pax Scientific, Inc | A vortical flow rotor |
| US8328522B2 (en) | 2006-09-29 | 2012-12-11 | Pax Scientific, Inc. | Axial flow fan |
| CN100595471C (en) * | 2007-06-15 | 2010-03-24 | 新疆石油管理局采油工艺研究院 | Steam distributor and symmetric steam-distributing pipeline and using method thereof |
| US20090308472A1 (en) * | 2008-06-15 | 2009-12-17 | Jayden David Harman | Swirl Inducer |
| US8695632B2 (en) * | 2011-10-18 | 2014-04-15 | Brinemaker, Inc. | Underground brine generating system |
| CN102777161A (en) * | 2012-06-18 | 2012-11-14 | 陕西得波材料科技有限公司 | Wing-shaped mixed-phase steam intake column uniform-dryness distributor |
| US9022066B2 (en) * | 2012-12-09 | 2015-05-05 | Christ Spoorenberg | Effluent flow splitter |
| US10900338B2 (en) * | 2014-10-29 | 2021-01-26 | Schlumberger Technology Corporation | System and method for dispersing fluid flow from high speed jet |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2144898A (en) * | 1938-04-07 | 1939-01-24 | Alco Valve Company Inc | Unitary expansion valve and distributor mechanism |
| US3899000A (en) * | 1973-09-20 | 1975-08-12 | Atlantic Richfield Co | Liquid-vapor distributor |
| US4269211A (en) * | 1979-02-05 | 1981-05-26 | Texaco Inc. | Steam manifold distribution system for providing equal quality of steam in two lines |
| US4528919A (en) * | 1982-12-30 | 1985-07-16 | Union Oil Company Of California | Multi-phase fluid flow divider |
| US4505297A (en) * | 1983-08-02 | 1985-03-19 | Shell California Production Inc. | Steam distribution manifold |
| US4574837A (en) * | 1983-09-29 | 1986-03-11 | Exxon Production Research Co. | Method and apparatus for splitting two-phase gas-liquid flows having a known flow profile |
| US4800921A (en) * | 1986-06-20 | 1989-01-31 | Exxon Production Research Company | Method and apparatus for dividing a single stream of liquid and vapor into multiple streams having similar vapor to liquid rations |
-
1990
- 1990-05-21 US US07/526,475 patent/US5010910A/en not_active Expired - Fee Related
-
1991
- 1991-05-07 CA CA002041979A patent/CA2041979A1/en not_active Abandoned
Also Published As
| Publication number | Publication date |
|---|---|
| US5010910A (en) | 1991-04-30 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FZDE | Discontinued |