JP2011169494A - Open rack-type vaporizer - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide an ORV including a lower header of a double pipe structure and capable of stabilizing an operation by suppressing fluctuation of a delivery flow rate of NG. <P>SOLUTION: In this ORV, a plurality of fin tubes 2 are arranged in a panel shape, an upper header 4 and the lower header 5 are respectively connected to upper and lower ends of the fin tubes, LNG supplied to the lower header 5 is introduced into the fin tubes 2 and vaporized, and NG is sent out from the upper header 4. The lower header 5 is constituted of an outer pipe 9 to which the lower ends of the fin tubes 2 are jointed and which is closed at both ends, and a sparger pipe 10 which is extended into the outer pipe 9, and closed by a closing plate 12 at its terminal end, and to which LNG is supplied from its starting end. The sparger pipe 10 is provided with LNG spreading holes 16 at its lower section and degassing holes 17 at its upper section, and is supported in the outer pipe 9 by a ring plate 19 disposed between joining sections of the outer pipe 9 and the fin tubes 2. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

  The present invention relates to an open rack type vaporizer (hereinafter referred to as “ORV”) used for vaporizing liquefied natural gas (hereinafter referred to as “LNG”) into natural gas (hereinafter referred to as “NG”).

LNG, since it does not contain sulfur as a main component methane, as clean fuel which does not emit environmental pollutants such as SO _X, is used in various industrial fields. LNG is brought into an ultra-low temperature liquefied state of about −160 ° C. at the place of production, and is transported to a demand place by a tanker. In order to use LNG as a fuel, it is necessary to vaporize it and return it to NG. Conventionally, ORV has been frequently used (see, for example, Patent Document 1).

  The ORV heats a heat exchange panel in which a plurality of heat transfer tubes are arranged in a panel shape, and headers are provided on the upper and lower ends thereof from the outside by a heat medium, and heats the LNG flowing through the heat transfer tubes to vaporize to NG. A type of exchanger.

  FIG. 1 is a diagram schematically showing a heat exchange panel constituting the main part of the ORV and equipment attached thereto. As shown in the figure, the heat exchange panel 1 is configured by arranging a plurality of fin tubes 2 in the radial direction and arranging them in a panel shape, and joining an upper header 4 and a lower header 5 to the upper end and the lower end, respectively. The fin tube 2 has a plurality of fins 3 protruding outward from the outer peripheral surface of the tube wall. The ORV is formed by arranging a large number of such heat exchange panels 1 in parallel according to specifications.

  An upper manifold 6 and a lower manifold 7 are connected to the upper header 4 and the lower header 5 of each heat exchange panel 1, respectively. Further, a trough 8 is disposed adjacent to the fin tube 2 at the top of each heat exchange panel 1. Seawater is supplied to the trough 8 as a heat medium, and the seawater overflows from the trough 8 and flows down the surface of the fin tube 2. Circulating water may be used as the heat medium.

  LNG is supplied to the lower header 5 through the lower manifold 7 and introduced into the fin tube 2. The LNG introduced into the fin tube 2 is vaporized by heat exchange with seawater flowing down the surface of the fin tube 2, and becomes NG and is led to the upper header 4. The NG led out to the upper header 4 is sent to the outside through the upper manifold 6.

  In the ORV, in order to evenly distribute the LNG supplied to the lower header 5 to all the fin tubes 2 from the start end to the end, the lower header 5 having a double pipe structure is often adopted.

  2A and 2B are views showing the vicinity of the terminal end of the lower header of the double pipe structure in the conventional ORV. FIG. 2A is a longitudinal sectional view, and FIG. 2B is AA of FIG. FIG. 4C is a cross-sectional view, and FIG. FIG. 3 is a longitudinal sectional view showing the vicinity of the manifold side of the lower header of the double pipe structure in the conventional ORV.

  As shown in FIGS. 2 and 3, the lower header 5 has a double-pipe structure, and includes an outer tube 9 and a sparge pipe 10 extending inside the outer tube 9. The outer tube 9 communicates with each fin tube 2 by joining the lower end of each fin tube 2 to the top of the tube wall by welding. The end of the outer tube 9 is closed by an end cap 11 having an inner space such as a hemispherical shape as shown in FIG. 2A, and its starting end is joined to the lower manifold 7 by welding as shown in FIG. Has been.

  The sparge pipe 10 is inserted into the outer tube 9 and assembled. The end of the sparge pipe 10 is closed by a closing plate 12 as shown in FIGS. A plate-like ring portion 13 projects from the outer periphery of the closing plate 12, and the sparge pipe 10 is supported in the outer tube 9 by the ring portion 13.

  As shown in FIG. 3, a ring plate 14 is attached to the outer periphery of the start end of the sparge pipe 10. The ring plate 14 plays a role of supporting the sparge pipe 10 in the outer pipe 9 in the vicinity of the lower manifold 7. Thus, an annular space 15 is formed between the tube walls of the outer tube 9 and the sparge pipe 10. The LNG that has passed through the lower manifold 7 is supplied into the sparge pipe 10 from the start end of the sparge pipe 10.

  In addition, in the lower part of the tube wall of the sparge pipe 10, LNG spray holes 16 are formed at predetermined intervals so that the LNG supplied to the inside of the sparge pipe 10 is uniformly distributed to the annular space 15 in the outer tube 9 and flows out. Has been. In general, as shown in FIG. 2C, the LNG spray hole 16 is provided at a position obliquely downward from the bottom to 85 ° or a position just beside 90 ° in the cross section of the sparge pipe 10.

  In the ORV including the lower header 5 having such a double pipe structure, when the LNG is introduced from the lower header 5 to the fin tube 2, the LNG is supplied to the sparge pipe 10 constituting the lower header 5, And flows out from the annular space 15 in the outer tube 9 almost uniformly. The LNG that has flowed into the annular space 15 is heated by heat input from seawater flowing down the surface of the fin tube 2 and reaching the outer surface of the outer tube 9, and is introduced into each fin tube 2 almost uniformly.

  In the lower header 5, part of the LNG may be vaporized by heat input from the seawater, and part of the LNG supplied to the sparge pipe 10 may also be vaporized in the sparge pipe 10. For this reason, a gas vent hole 17 </ b> A is formed at the top of the tube wall of the sparge pipe 10. This degassing hole 17 </ b> A fulfills a degassing function for releasing NG in the sparge pipe 10 into the annular space 15. A gas vent hole 17B is also formed in the upper part of the closing plate 12 that closes the end of the sparge pipe 10. The gas vent hole 17 </ b> B performs a gas vent function for discharging NG in the sparge pipe 10 to the terminal space 18 formed by the closing plate 12, the ring portion 13, and the end cap 11.

JP 2000-28276 A (paragraphs 0003 to 0004)

  Since ORV flows from the liquid phase to the gas phase through the mixed phase of the liquid phase and the gas phase, the ORV internally flows with the possibility of fluctuations in pressure and flow rate. . Normally, the fluctuation does not become a magnitude that hinders the operation, but if special problems such as the flow rate control method are combined, the NG flow rate at the ORV outlet may fluctuate greatly and become rare. is there. When significant fluctuations occur in the NG delivery flow rate, stable operation becomes difficult.

  The present invention has been made in view of the above problems, and an object of the present invention is to provide an ORV that includes a lower header having a double-pipe structure and that can suppress fluctuations in the flow rate of NG and can realize operation stabilization. And

  In order to achieve the above-described object, the present inventors have made extensive studies on the factors that cause fluctuations in the delivery flow rate of NG on the premise of adopting a lower header having a double-pipe structure. The knowledge of e) was obtained.

FIG. 4 is a diagram for explaining the behavior of the LNG near the end of the conventional lower header.
(A) As shown in FIG. 4, the LNG supplied into the sparge pipe 10 flows out from each LNG spray hole 16 and flows into the annular space 15. The LNG in the annular space 15 rises toward the fin tube 2, but the temperature is raised by heat input from the seawater, and part of the gas may evaporate depending on the conditions. In that case, the LNG and NG mixed phase flow And is introduced into the fin tube 2. In addition, NG vaporized in the sparge pipe 10 is discharged from the gas vent hole 17A, flows into the annular space 15, and joins the mainstream. At this time, the terminal space 18 is isolated by the ring portion 13 protruding from the outer periphery of the closing plate 12, but there is a slight gap between the outer peripheral surface of the ring portion 13 and the inner peripheral surface of the outer tube 9. Therefore, a part of the LNG in the annular space 15 enters the terminal space 18 through the gap and stays there.

  A part of the LNG staying in the terminal space 18 is vaporized by heat input from seawater. In addition, NG vaporized in the sparge pipe 10 is discharged from the gas vent hole 17B and flows into the terminal space 18. . These NGs also flow out into the annular space 15 from a slight gap between the outer peripheral surface of the ring portion 13 and the inner peripheral surface of the outer tube 9, and merge into the mainstream. However, since the circulation between the terminal space 18 and the annular space 15 is very small, the terminal space 18 can be said to be in a semi-closed state.

  (B) When the LNG flow rate is low or the heat input from seawater is large, the liquid level exists in the sparge pipe 10 or in the annular space 15 and the terminal space 18 and there are many places where LNG and NG are mixed, It is in a state where the pressure is balanced, and the two-phase flow of LNG and NG flows stably as such.

  (C) When the LNG flow rate increases or the heat input from the seawater decreases and the sparge pipe 10 is almost filled with LNG, the LNG and NG are mixed only in the vicinity of the end in the sparge pipe 10. NG and NG may alternately flow into the terminal space 18 from the vent hole 17B.

  Since the volume ratio per unit weight is greatly different between LNG and NG, when LNG and NG alternately flow into the semi-closed terminal space 18, the pressure in the terminal space 18 varies slightly. If a pressure pulsation having substantially the same periodicity is applied to the LNG upstream side piping or the like, resonance may result in large pressure fluctuations. Since this pressure is a power source for causing NG to flow out from a slight gap between the outer peripheral surface of the ring portion 13 and the inner peripheral surface of the outer tube 9, the amount of NG outflow passing through the gap due to the influence of pressure fluctuations. As a result, the LNG level fluctuation occurs in the terminal space 18. At this time, NG in the terminal space 18 and the annular space 15 becomes a compressive capacity, so that the pressure fluctuation is propagated also in the sparge pipe 10 and the annular space 15, and a large liquid level fluctuation occurs in the entire inside of the outer pipe 9. It may become a state to do. This liquid level fluctuation and pressure fluctuation induce fluctuations in the LNG flow rate and pressure flowing into the fin tube 2, and may eventually be detected as fluctuations in the NG delivery flow rate and pressure at the ORV outlet.

  (D) When the LNG flow rate increases further than in the case of (c) above, or the heat input from seawater decreases and the sparge pipe 10 and the terminal space 18 are completely filled with LNG, Since only LNG flows into the terminal space 18, the sparge pipe 10 and the terminal space 18 are in a stable state in which the pressure is balanced, and the liquid level fluctuation of the LNG converges.

  (E) Normally, even if the liquid level fluctuation occurs as in (c) above, the ORV operation is not hindered. However, if the flow control device upstream of the ORV is too sensitive to fluctuations in NG pressure or delivery flow, the fluctuations are not suppressed well, and the fluctuations are promoted on the contrary, and the flow rate is such that operational problems occur. Sometimes it develops into variation.

  Based on the findings of (a) to (e), the present inventors smoothly circulate LNG and NG through the annular space and the terminal space in the outer tube in order to suppress fluctuations in the NG delivery flow rate. With this structure, even if pressure pulsation is caused from the upstream side of the ORV, it becomes difficult to cause resonance, and it has been found that it is effective to suppress the liquid level fluctuation of the LNG in the outer tube. Completed.

  The gist of the present invention resides in the following ORV. That is, a plurality of fin tubes are arranged in a panel shape, and upper and lower headers are joined to the upper and lower ends, respectively, and LNG supplied to the lower header is introduced into the fin tube to vaporize the vaporized NG. In the ORV sent from the upper header, the lower header is joined to the lower end of each fin tube, the outer tube is closed at both ends, and extends to the inside of the outer tube. The sparge pipe is provided with an LNG spray hole at the lower part of the tube wall, a gas vent hole at the upper part of the tube wall, and the joints between the outer tube and the fin tube The ORV is characterized in that it is supported in the outer tube by a ring plate disposed between the two.

  In the ORV, the end of the outer tube is closed by an end cap, and the maximum distance in the axial direction of the outer tube between the inner surface of the end cap and the outer surface of the closing plate is less than half of the inner diameter of the outer tube. A certain configuration is preferable.

  In the ORV described above, it is preferable that the gas vent hole is provided close to the blocking plate and provided at an upper position within a range of 85 ° from the top in the cross section of the sparge pipe.

  According to the ORV of the present invention, the terminal space formed by the closing plate and the end cap communicates with the annular space in the outer pipe without being isolated, and is discharged from the LNG flowing out from the LNG spraying hole and the gas venting hole. The generated NG does not stay in the terminal space. For this reason, since NG vaporized in the terminal space flows smoothly into the annular space, the liquid level fluctuation of the LNG can be suppressed in the annular space, and as a result, the fluctuation in the flow rate of NG sent through the upper header is reduced. It is possible to stabilize the operation.

It is a figure which shows typically the heat exchange panel which comprises the principal part of ORV, and the equipment incidental to it. It is a figure which shows the terminal vicinity vicinity of the lower header of the double pipe structure in the conventional ORV, The figure (a) is a longitudinal cross-sectional view, The figure (b) is AA sectional drawing of the figure (a), FIG. 6C shows a cross-sectional view taken along the line BB of FIG. It is a longitudinal cross-sectional view which shows the manifold side vicinity of the lower header of the double pipe structure in the conventional ORV. It is a figure explaining the behavior of LNG in the terminal vicinity vicinity of the conventional lower header. It is a figure which shows the termination | terminus vicinity of the lower header of the double pipe structure in ORV of this invention, The figure (a) is a longitudinal cross-sectional view, The figure (b) is CC sectional drawing of the figure (a). (C) shows a DD cross-sectional view of FIG. (A), and (d) shows an EE cross-sectional view of (a).

Hereinafter, embodiments of the ORV of the present invention will be described in detail with reference to the drawings.
FIG. 5 is a view showing the vicinity of the terminal end of the lower header of the double pipe structure in the ORV of the present invention, where FIG. 5 (a) is a longitudinal sectional view, and FIG. FIG. 4C is a sectional view taken along line C, FIG. 5C is a sectional view taken along line DD in FIG. 4A, and FIG. 4D is a sectional view taken along line EE in FIG. The lower header shown in the figure and the ORV including the same are based on the configuration of the lower header shown in FIGS. 2 and 3 and the ORV shown in FIG. 1 provided with the same, and the same components are denoted by the same reference numerals. The overlapping description will be omitted as appropriate.

  As shown in FIG. 5, the lower header 5 in the ORV of the present invention includes an outer tube 9 in which the lower end of each fin tube 2 is joined to the top of the tube wall by welding, and extends inside the outer tube 9. The sparge pipe 10 is provided with a LNG spray hole 16 formed in the lower portion of the tube wall.

  As shown in FIGS. 5A and 5B, the end of the sparge pipe 10 is closed by a closing plate 12. The closing plate 12 has a disk shape having the same diameter as the outer diameter of the sparge pipe 10 and does not have the ring portion 13 like the conventional lower header shown in FIGS.

  A ring plate 19 is attached to the outer periphery of the sparge pipe 10 as shown in FIGS. The ring plate 19 is disposed between the joint portions of the outer tube 9 and the fin tube 2, and supports the sparge pipe 10 in the outer tube 9 instead of the ring portion 13.

  In the present embodiment, as shown in FIG. 5A, a dish-shaped end plate having a dish-shaped internal space is employed as the end cap 11 that closes the end of the outer tube 9. The end of the sparge pipe 10 closed by the closing plate 12 is disposed close to the end cap 11.

  Further, as shown in FIGS. 5A and 5C, the sparge pipe 10 of the present embodiment is provided with a gas vent hole 17C in the upper part of the tube wall in the vicinity of the closing plate 12. The degassing holes 17C are not particularly limited as long as they are located in the upper half region of the cross section of the sparge pipe 10, but there are no particular restrictions on the position and the number of degassing holes. It is preferably provided at a position obliquely above within the range of °. More preferably, it is within a range of 45 ° from the top. The diameter of the vent hole 17C is preferably about 4 to 20 mm.

  In the ORV including the lower header 5 having such a configuration, the closing plate 12 that closes the end of the sparge pipe 10 does not have the ring portion 13 and is disposed between the joint portions of the outer tube 9 and the fin tube 2. Since the sparging pipe 10 is supported by the ring plate 19 formed, the terminal space 18 formed by the closing plate 12 and the end cap 11 communicates with the annular space 15 in the outer tube 9 without being isolated. . As a result, the LNG supplied into the sparge pipe 10 flows out from each LNG spray hole 16 and flows into the annular space 15, and further smoothly flows into the terminal space 18. In addition to this, NG vaporized in the sparge pipe 10 is discharged from the gas vent hole 17 </ b> C, fills the annular space 15, and flows smoothly into the terminal space 18. That is, LNG and NG do not stay in the terminal space 18.

  For this reason, even when LNG present in the terminal space 18 is vaporized, the vaporized NG smoothly flows into the annular space 15 and is introduced into each fin tube 2, so that the NG in the terminal space 18 is compressed. Therefore, the LNG liquid level fluctuation can be suppressed in the annular space 15. Thereby, as the pressure of the annular space 15 is stabilized and the flow rate of the LNG in the gas-liquid mixed state introduced into each fin tube 2 is stabilized, the inside of the outer tube 9 as described in the above knowledge (c). It is possible to reduce fluctuations in the flow rate of NG sent out through the upper header 4 as compared with a case where a large liquid level fluctuation occurs as a whole. As a result, even if the flow rate control device as described in the above knowledge (e) is adopted, it is possible to realize stabilization of operation.

  Further, by using the end cap 11 having a dish-shaped or semi-elliptical inner space, the end cap used in the conventional lower header shown in FIGS. 2 and 4, that is, a hemispherical inner space is used. The volume of the terminal space 18 can be reduced to half or less, and the effect of suppressing the LNG liquid level fluctuation in the annular space 15 is further enhanced. In this case, the maximum distance in the axial direction of the outer tube 9 between the inner surface of the end cap 11 and the outer surface of the closing plate 12 is set to be half or less of the inner diameter of the outer tube 9. For example, when the inner diameter of the outer tube 9 is 140 mm, the maximum distance between the inner surface of the end cap 11 and the outer surface of the closing plate 12 is 70 mm or less. As long as it is within this range, the shape of the end cap 11 is not limited, and the inside of the end cap 11 may be filled.

  In addition, the degassing function can be effectively exhibited by providing the degassing hole 17C close to the closing plate 12 and at an obliquely upper position within a range of 85 ° from the top in the cross section of the sparge pipe 10. Moreover, the occurrence of through cracks can be prevented at the joint between the outer tube 9 and the fin tube 2. The latter effect is due to the following reason.

  From the gas vent hole 17C, NG vaporized in the sparge pipe 10 is released, and LNG is also released. For this reason, depending on the operating conditions, NG and low-temperature LNG may be alternately ejected from the vent hole 17C, and a discontinuous shape such as a joint between the outer tube 9 and the fin tube 2 exists at the ejection destination. In such a case, thermal stress is repeatedly generated in the portion, but the thermal stress is significantly larger than that of the smooth surface due to the stress concentration, so that there is a risk that through cracks may occur due to fatigue failure with long-term operation.

  As in the lower header 5 of the present embodiment, if the gas vent hole 17C is provided close to the closing plate 12 and is provided at an obliquely upper position in the cross section of the sparge pipe 10, the gas vent hole 17C is connected to the outer tube 9. Since the NG and the LNG ejected from the degassing holes 17C do not reach the joint portion directly because they are arranged at positions deviated from the joint portion with the fin tube 2, repeated thermal stress induces a through crack. Does not occur.

  In addition, the present invention is not limited to the above-described embodiment, and various modifications can be made without departing from the spirit of the present invention.

  According to the ORV of the present invention, the LNG flowing out from the LNG spray hole and the NG released from the gas vent hole do not stay in the terminal space in the end cap. As the air flows into the space, it is possible to suppress the LNG liquid level fluctuation in the annular space, and as a result, it is possible to prevent fluctuations in the flow rate of NG sent through the upper header and to stabilize the operation. It becomes possible to do.

1: heat exchange panel, 2: fin tube, 3: fin,
4: Upper header, 5: Lower header, 6: Upper manifold,
7: Lower manifold, 8: Trough, 9: Outer pipe,
10: Sparge pipe, 11: End cap, 12: Blocking plate,
13: ring part, 14: ring plate, 15: annular space,
16: LNG spray hole, 17A, 17B, 17C: vent hole,
18: Termination space, 19: Ring plate

Claims (3)

A plurality of fin tubes are arranged in a panel shape, and upper and lower headers are joined to the upper and lower ends, respectively. LNG supplied to the lower header is introduced into the fin tube and vaporized, and the vaporized NG is upper header. In the open rack type vaporizer sent out from
The lower header has an outer tube in which the lower ends of the fin tubes are joined and closed at both ends, and a sparge pipe that extends into the outer tube, is closed with a closing plate and is supplied with LNG from the starting end, Consisting of
The sparge pipe is provided with an LNG spray hole in the lower part of the pipe wall, and a gas vent hole in the upper part of the pipe wall. The sparge pipe has a ring plate arranged between the joints of the outer pipe and the fin tube. Open rack type vaporizer characterized by being supported by.   The end of the outer tube is closed by an end cap, and the maximum distance in the axial direction of the outer tube between the inner surface of the end cap and the outer surface of the closing plate is less than half of the inner diameter of the outer tube. The open rack type vaporizer according to claim 1.   3. The open according to claim 1, wherein the vent hole is provided close to the blocking plate and at an upper position within a range of 85 ° from the top in the cross section of the sparge pipe. Rack type vaporizer.

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