Mitigation of Shell-Side Liquid Maldistribution in Coil Wound Heat Exchanger Bundles
20230147084 · 2023-05-11
Assignee
Inventors
- Bo Jin (Orefield, PA, US)
- Justin David Bukowski (Hamburg, PA, US)
- Patrick Alan Houghton (Emmaus, PA, US)
- Christopher Michael Ott (Macungie, PA, US)
- Mark Julian Roberts (Whitehall, PA, US)
- Mark Robert Pillarella (Center Valley, PA, US)
Cpc classification
F28D7/022
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25J1/0022
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25J1/021
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F28D7/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25J1/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
Described herein are coil wound heat exchangers (CWHEs), and methods of cooling and/or liquefying streams of fluid using said CWHEs, in which one or more tube layers of the tube bundle are provided with a non-uniform tube winding angle and tube pitch in order to facilitate the equalization of radial pressure imbalances on the shell side of the CWHE, thereby reducing radial maldistribution of fluid on the shell side and improving the heat transfer efficiency of the CWHE.
Claims
1. A coil wound heat exchanger (CWHE) comprising a tube bundle enclosed within a pressure vessel, the tube bundle comprising a plurality of tubes for conveying one or more streams of fluid in heat exchange with a fluid flowing through the pressure vessel externally to the tubes, said tubes being helically wound about a mandrel extending in an axial direction of the bundle so as to form a plurality of tube layers around said mandrel, each of said tube layers comprising one or more of said helically wound tubes, wherein at least one of the tube layers has a first tube winding angle and a first tube pitch at a first axial location of the layer towards one axial end of the bundle, a second tube winding angle and a second tube pitch at a second axial location of the layer towards the opposite axial end of the bundle, and a third tube winding angle and third tube pitch at a third axial location of the layer between the first axial location and second axial location, the third tube winding angle being greater than the first tube winding angle and greater than the second tube winding angle and the third tube pitch being greater than the first tube pitch and greater than the second tube pitch.
2. A CWHE as claimed in claim 1, wherein all or substantially all of the tube layers have a first tube winding angle and a first tube pitch at a first axial location of the layer towards one axial end of the bundle, a second tube winding angle and a second tube pitch at a second axial location of the layer towards the opposite axial end of the bundle, and a third tube winding angle and third tube pitch at a third axial location of the layer between the first axial location and second axial location, for each of said layers the third tube winding angle being greater than the first tube winding angle and greater than the second tube winding angle and the third tube pitch being greater than the first tube pitch and greater than the second tube pitch.
3. A CWHE as claimed in claim 2, wherein the third axial locations of each of said tube layers are at the same or substantially the same axial position of the bundle.
4. A CWHE as claimed in claim 1, wherein in at least one of or all or substantially all of the tube layers the third tube winding angle at the third axial location is equal to or larger than any tube winding angle at any other axial location of the layer between the first axial location and the second axial location of the layer, and the third tube pitch at the third axial location is equal to or greater than any tube pitch at any other axial location of the layer between the first axial location and the second axial location of the layer.
5. A CWHE as claimed in claim 1, wherein in at least one of or all or substantially all of the tube layers the third axial location of the layer is at a point that falls between 10% and 90% of the distance in the axial direction of the bundle between the first axial location and second axial location.
6. A CWHE as claimed in claim 1, wherein in at least one of or all or substantially all of the tube layers the third tube winding angle is at least 5% greater than the first tube winding angle and at least 5% greater than the second tube winding angle.
7. A CWHE as claimed in claim 1, wherein in at least one of or all or substantially all of the tube layers the third tube winding angle is at least 0.5 degrees greater than the first tube winding angle and is at least 0.5 degrees greater than the second tube winding angle.
8. A CWHE as claimed in claim 1, wherein in at least one of or all or substantially all of the tube layers the third tube pitch is at least 5% greater than the first tube pitch and is at least 5% greater than the second tube pitch.
9. A CWHE as claimed in claim 1, wherein in at least one of or all or substantially all of the tube layers the third tube pitch is at least 10% greater than the first tube pitch and is at least 10% greater than the second tube pitch.
10. A CWHE as claimed in claim 1, wherein the CWHE is a vertically oriented CWHE with the axial direction of the bundle being vertical or substantially vertical, the CWHE further comprising a refrigerant dispenser located above the tube bundle for dispensing a refrigerant into the pressure vessel externally to the tubes so that the refrigerant flows downwards through the pressure vessel over and through the tube bundle externally to the tubes.
11. A CWHE as claimed in claim 10, wherein the CWHE has an inlet configured to introduce the one or more streams of fluid into the plurality of tubes of the tube bundle at the bottom of the tube bundle and an outlet configured to withdraw the one or more streams of fluid from the tubes at the top of the tube bundle such that the one or more streams flow upwards through the tubes of the tube bundle.
12. A CWHE as claimed in claim 10, wherein the CWHE is configured to use a liquid or two-phase refrigerant that vaporizes as it flows downwards through the pressure vessel over and through the tube bundle externally to the tubes.
13. A method of cooling and/or liquefying one or more streams of fluid via heat exchange with a refrigerant using a CWHE as claimed in claim 1, wherein the method comprises passing the one or more streams of fluid through the plurality of tubes of the tube bundle and passing the refrigerant through the pressure vessel externally to the tubes.
14. The method of claim 13, wherein the one or more streams of fluid that are to be cooled and/or liquefied comprise a natural gas stream.
15. The method of claim 13, wherein the refrigerant comprises a mixed refrigerant.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DETAILED DESCRIPTION
[0045] Described herein are coil wound heat exchangers, and methods of cooling and/or liquefying streams of fluid using said coil wound heat exchangers, in which one or more tube layers of the tube bundle are provided with a non-uniform tube winding angle and tube pitch in order to facilitate the equalization of radial pressure imbalances on the shell side of the coil wound heat exchanger (CWHE), thereby reducing radial maldistribution of fluid (particularly liquid) on the shell side of the CWHE and improving the heat transfer efficiency of the CWHE in operation.
[0046] As used herein and unless otherwise indicated, the articles “a” and “an” mean one or more when applied to any feature in embodiments of the present invention described in the specification and claims. The use of “a” and “an” does not limit the meaning to a single feature unless such a limit is specifically stated. The article “the” preceding singular or plural nouns or noun phrases denotes a particular specified feature or particular specified features and may have a singular or plural connotation depending upon the context in which it is used.
[0047] Where used herein to identify recited features of a method or system, the terms “first”, “second”, “third” and so on, are used solely to aid in referring to and distinguishing between the features in question, and are not intended to indicate any specific order of the features, unless and only to the extent that such order is specifically recited.
[0048] As used herein, the “tube winding angle” of a tube of a tube layer at a particular location refers to the included (acute) angle formed between the tube axis of the tube at that location and a plane perpendicular to the tube bundle axis. The tube winding angle of a tube layer at a particular axial location refers, where the layer is formed of a single tube, to the tube winding angle of the tube of the layer at that axial location or refers, where the layer is formed of more than one tube, to the average (arithmetic mean) of the tube winding angles of the tubes of the layer at that axial location.
[0049] As used herein, the “tube pitch” of a tube of a tube layer at a particular location refers to the average (arithmetic mean) of the center-to-center distances between the tube axis of the turn of the tube at that location and tube axes of each of the two adjacent turns of tube in the layer, the center-to-center distance between two turns of tube being measured perpendicular to the axes of the turns of tubes in question. Depending on the number of tubes that form the tube layer, the two turns of tube that are adjacent to the turn of tube at the location in question may be turns of the same tube or turns of a different tube or pair of tubes. More specifically, where the tube layer is formed of a single tube, the two turns of tube that are adjacent to the turn of a tube at a particular location will be the two adjacent turns of the same single tube that forms the layer; where the tube layer is formed of two tubes, the two turns of tube that are adjacent to the turn of a tube at a particular location will be the two adjacent turns of the other tube forming the layer; and where the tube layer is formed of three or more tubes, the two turns of tube that are adjacent to the turn of a tube at a particular location will be the adjacent turns of the adjacent tubes in the layer. The tube pitch of a tube layer at a particular axial location refers, where the layer is formed of a single tube, to the tube pitch of the tube of the layer at that axial location or refers, where the layer is formed of more than one tube, to the average (arithmetic mean) of the tube pitches of the tubes of the layer at that axial location.
[0050] As used herein, the “tube axis” of a tube or the turn of a tube refers to the central longitudinal axis of said tube or turn of tube.
[0051] As used herein, the “tube bundle axis” refers to the central longitudinal axis of the tube bundle. Typically, the tube layers of the tube bundle form a set layers positioned coaxially about the mandrel, such that the tube bundle and mandrel share the same central longitudinal axis (within manufacturing tolerances). Typically, the pressure vessel that contains the tube bundle is a generally cylindrical vessel that is likewise positioned coaxially with the tube layers and mandrel.
[0052] As used herein, the “axial direction of the bundle” refers to the direction along the tube bundle axis; an “axial location” or “axial position” of the bundle refers to a location or position that is at a specific point along the tube bundle axis, but (unless otherwise indicated) does not refer to any specific circumferential location of the tube bundle at that axial point along the tube bundle axis; and the “axial ends” of the bundle refer to the ends of the bundle at either end of the tube bundle axis.
[0053] Solely by way of example, certain exemplary embodiments of the invention will now be described with reference to the Figures.
[0054] As described above, a coil wound heat exchanger (CWHE) is a type of heat exchanger that is well known in the art and that can be fabricated by methods that are well known in the art. A CWHE comprises one or more tube bundles that are enclosed within a pressure vessel, the or each tube bundle comprising a plurality of tubes suitable for conveying one or more streams of fluid in heat exchange with a fluid flowing through the pressure vessel externally to the tubes. The tubes of the or each tube bundle are helically wound about a mandrel that extends in an axial direction of the bundle such that said tubes form a plurality of tube layers around said mandrel, each of said tube layers comprising one or more of said helically wound tubes. Typically, each tube layer is spaced from adjacent tube layers (i.e. separated in the radial direction of the bundle) by spacers, which may for example take the form of spacer wires or rods. At each axial end of the tube bundle the ends or “tails” of the one or more helically wound tube or tubes forming each tube layer are typically aggregated or gathered together into one or more groups with the end or “tails” of the tubes forming the other layers so that each tail in the group can be inserted and fixed into a tube sheet, so as to thereby form a group of inlets or outlets. The one or more tube bundles can be installed in the pressure vessel with appropriate headers and piping for introducing one or more streams of fluid into the tubes and withdrawing said stream(s) from the tubes, via said inlets and outlets, and additional piping may be used for fluid flow between bundles.
[0055] In many instances coil wound heat exchangers are used for cooling and/or liquefying one or more streams of fluid, with said stream(s) of fluid being passed through the tubes of the one or more tube bundles of the CWHE (i.e. through the “tube-side” of the CWHE), and with a cold refrigerant being passed through the pressure vessel externally to the tubes (i.e. through the shell-side of the CWHE). Often, the CWHE is employed in a “cold end up” orientation, whereby the CWHE is vertically oriented with the tube bundle axis being vertical or substantially vertical, the CWHE having a refrigerant dispenser located above the or each tube bundle (or located above at least the top most bundle in the event that more than one bundle is present) for dispensing a refrigerant into the pressure vessel externally to the tubes so that the refrigerant flows downwards through the pressure vessel over and through the tube bundle(s) externally to the tubes, and the CWHE being configured such that the one or more streams of fluid that are to be cooled and/or liquefied are introduced at the bottom of the tube bundle(s), flow upwards through the tubes of the tube bundle(s), and are withdrawn from the top of the tube bundle(s). Often the CWHE is configured to use a liquid or two-phase refrigerant that vaporizes as it flows downwards through the pressure vessel over and through the tube bundle externally to the tubes.
[0056] Such coil wound heat exchangers can be used in a variety of different processes, but in certain preferred embodiments of the present invention they may be used for cooling and/or liquefying a natural gas stream using a mixed refrigerant. A suitable exemplary arrangement of a CWHE for liquefying a natural gas stream is shown in
[0057] In the typical prior art CWHE, the tube(s) in each tube layer have a uniform tube winding angle and tube pitch throughout the layer, as is illustrated in further detail by
[0058] More specifically,
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[0060] In a CWHE tube bundle, heat transfer occurs between the tube side stream(s) and shell side stream (as noted above), and uniform distribution of streams in both shell-side and tube-side is necessary in order to achieve the best heat transfer performance. However, it is known that radial maldistribution of fluid may occur in the shell-side of typical prior art CWHEs where the shell-side stream has two-phase flow (i.e. contains both liquid and vapor phases). More specifically, pressure imbalance can occur in the shell-side of the CWHE in the radial direction of the tube bundle when shell-side vapor and liquid concurrently flow downward over the tubes of the tube bundle, and this radial pressure imbalance can divert liquid on the shell-side in the radial direction of the tube bundle, resulting in liquid maldistribution on the shell-side of the CWHE. Such maldistribution not only reduces the heat transfer efficiency of the CWHE in operation, but also may force the use of a larger CWHE with a greater heat transfer surface area than theoretically required in order to allow for losses in heat transfer efficiency in practice.
[0061] The present inventors have now found that such radial pressure imbalances on the shell side of the CWHE can be equalized, and radial maldistribution of liquid on the shell side of the CWHE thereby reduced and the heat transfer efficiency of the CWHE thereby improved, by modifying the design of the CWHE tube bundle such that the CWHE uses instead tube bundle(s) in which one or more (and preferably all or substantially all) of the tube layers of the tube bundle have a non-uniform tube pitch, whereby the CWHE has a greater tube pitch at a middle location (axially) of the tube bundle than at locations towards the axial ends of the bundle. This non-uniform tube pitch is achieved by forming the or each of said tube layers from one or more tubes that have a non-uniform tube winding angle, whereby the tube layer(s) have a greater tube winding angle at a middle location (axially) of the tube bundle than at locations towards the axial ends of the bundle. This is because, for a given helically wound tube, increasing the winding angle of said tube increases the center-to-center distance between the turns of that tube. Thus, a greater tube winding angle at a particular location can provide a greater tube pitch at that location.
[0062] Accordingly, the coil wound heat exchangers according to the present invention differ from the typical prior art CWHE in that in a CWHE according to the present invention at least one of (and preferably all or substantially all of) the tube layers of the tube bundle have a first tube winding angle and a first tube pitch at a first axial location of the layer towards one axial end of the bundle, a second tube winding angle and a second tube pitch at a second axial location of the layer towards the opposite axial end of the bundle, and a third tube winding angle and third tube pitch at a third axial location of the layer between the first axial location and second axial location, the third tube winding angle being greater than the first tube winding angle and greater than the second tube winding angle and the third tube pitch being greater than the first tube pitch and greater than the second tube pitch.
[0063] The non-uniform tube pitch in the coil wound heat exchangers according to the present invention takes account of the variation in liquid to vapor ratio in the two-phase shell side fluid as it flows through the shell side in the axial direction of the tube bundle. In a vertically oriented CWHE, the two-phase shell side flow at the top of bundle contains little vapor and a large amount of liquid, while the two-phase shell side flow at the bottom of bundle contains little or no liquid and large amounts of vapor. The strongest vapor and liquid interaction occurs in the middle of bundle where the two-phase shell side flow contains comparable amounts of vapor and liquid. This strongest vapor and liquid interaction with heat transfer can generate the greatest radial pressure imbalance in the shell-side, which, in turn, drives the most severe liquid maldistribution therein. However, a larger tube pitch and hence a larger spacing between adjacent turns of tube has been found to equalize the radial pressure imbalance more effectively. Thus, a larger tube pitch in the middle of bundle has been found to better equalize the greater radial pressure imbalance at the middle of the bundle, hence providing better performance.
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[0065] More specifically,
[0066] As can be seen, in this exemplary embodiment both the winding angle and pitch of the helically wound tube forming the tube layer gradually increase moving (in the axial direction bundle) from the first axial location of the tube layer to a third axial location at which the tube winding angle and tube pitch reach a maximum, which third axial location falls, in this particular example, at a point that is 0.4 (i.e. 40% or ⅖.sup.th) of the total axial distance from the first axial location to the second axial location. Both the winding angle and pitch of the helically wound tube forming the tube layer then gradually decrease moving (in the axial direction bundle) from the third axial location of the tube layer to the second axial location of the tube layer. In this particular example the normalized tube pitch at the first axial location (i.e. the first tube pitch) is by definition 1.0 and the normalized tube winding angle at the first axial location (i.e. the first tube winding angle) is also 1.0, the normalized tube pitch at the second axial location (i.e. the second tube pitch) is 0.925 and the normalized tube winding angle at the second axial location (i.e. the second tube winding angle) is nearly the same value, and the normalized tube pitch at the third axial location (i.e. the third tube pitch) is 1.11 and the tube winding angle at the third axial location (i.e. the third tube winding angle) is nearly the same value. The normalized winding angle is close to the normalized tube pitch because at the small winding angles used for this example, less than 20°, the relationship between pitch and winding angle is nearly linear. At larger winding angles the value of normalized winding angle will differ by greater amount from the normalized tube pitch, but the shape of one curve will be similar to the other.
[0067] It should be noted that the specific distance of the third axial location from the first and second axial locations and specific tube pitch and tube winding angles in the above embodiment represent only one exemplary set of values, and other values may suitably be employed. However, it is preferred, in this and other embodiments of the invention: that the third axial location of the layer at which the tube winding angle and tube pitch are each at a maximum is at a point that falls between 10% and 90%, and more preferably between 20% and 80% or between 30% and 70%, of the distance in the axial direction of the bundle between the first axial location and second axial location; that the third tube winding angle is at least 5% greater than the first tube winding angle and at least 5% greater the second tube winding angle, and/or is at least 0.5 degrees greater than the first tube winding angle and is at least 0.5 degrees greater the second tube winding angle; and that the third tube pitch is at least 5% greater, and more preferably at least 10% greater than the first tube pitch and is at least 5% greater, and more preferably at least 10% greater than the second tube pitch. Typically, the tube layer will have (at any location of the between the first axial location and the second axial location) a minimum tube winding angle of 2°, a maximum tube winding angle of 25°, and a maximum tube pitch of 2.0 times the tube diameter.
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[0070] More specifically,
[0071] As can be seen, in this exemplary embodiment both the winding angle and pitch of the helically wound tube forming the tube layer initially remain constant, staying the same from the first axial location of the tube layer to a fourth axial location that is, in this particular example, at a point that is 20% of the total axial distance from the first axial location to the second axial location. At this fourth axial location, both the winding angle and pitch of the tube undergo a step change to a higher (maximum) value, and then remain at this higher (maximum) value until a fifth axial location that is, in this particular example, at a point that is 60% of the total axial distance from the first axial location to the second axial location. At this fifth axial location, both the winding angle and pitch of the tube undergo another step change, this time to a lower value, and remain at this lower value from the fifth axial location to the second axial location of the tube layer. Accordingly, in this embodiment, the third axial location of the tube layer, at which the tube winding angle and tube pitch are each at a maximum, can be considered to be any of the axial locations between the fourth axial location and fifth axial location. In this particular example the normalized tube pitch at the first axial location (i.e. the first tube pitch) is 1.0 and the normalized tube winding angle at the first axial location (i.e. the first tube winding angle) is 1.0, the normalized tube pitch at the second axial location (i.e. the second tube pitch) is 1.0 and the normalized tube winding angle at the second axial location (i.e. the second tube winding angle) is 1.0, and the normalized tube pitch at the third axial location (i.e. the third tube pitch) is 1.07 and the normalized tube winding angle at the third axial location (i.e. the third tube winding angle) is about 1.07.
[0072] It should be noted that the specific distance of the fourth and fifth axial locations (and hence third axial location) from the first and second axial locations, and the specific tube pitch and tube winding angles in the above embodiment represent only one exemplary set of values, and other values may suitably be employed, as discussed above in relation to the embodiment of the invention described with reference to
[0073] It should also be noted that in further embodiments of the invention a CWHE can be used that has a tube layer with a variation in tube pitch and tube winding angle that is a mixture of the variations in tube pitch and tube winding angle depicted in
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[0076] As can be seen from
[0077] It should be noted that although the tube layer in this exemplary embodiment is formed of fourteen tubes, in other embodiments higher or lower numbers of tubes could equally be used. Likewise, the specific distance of the fourth and fifth axial locations (and hence third axial location) from the first and second axial locations, and the specific tube pitch and tube winding angles used in the above embodiment represent only one exemplary set of values, and other values may suitably be employed, as discussed above in relation to the embodiment of the invention described with reference to
[0078]
[0079]
[0080] As can be seen from
[0081] Again, although the tube layer in this exemplary embodiment is formed of fourteen tubes, in other embodiments higher or lower numbers of tubes could equally be used. Likewise, the specific distance of the third, fourth and fifth axial locations from the first and second axial locations, and the specific tube pitches and tube winding angles used in the above embodiment represent only one exemplary set of values, and other values may suitably be employed, as discussed above in relation to the embodiment of the invention described with reference to
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[0084] As can be seen from
[0085] It should be noted that although the tube layer in this exemplary embodiment is formed of fourteen tubes, in other embodiments higher or lower numbers of tubes could equally be used. Likewise, the specific distances of the fourth, fifth, sixth and seventh axial locations (and hence third axial location) from the first and second axial locations, and the specific tube pitch and tube winding angles used in the above embodiment represent only one exemplary set of values, and other values may suitably be employed, as discussed above in relation to the embodiment of the invention described with reference to
[0086] In each of the embodiments of the invention described above with reference to
[0087] It will be appreciated that the invention is not restricted to the details described above with reference to the preferred embodiments but that numerous modifications and variations can be made without departing from the spirit or scope of the invention as defined in the following claims.