JP2017078475A - Intermediate medium type gas vaporizer - Google Patents

Intermediate medium type gas vaporizer Download PDF

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JP2017078475A
JP2017078475A JP2015207135A JP2015207135A JP2017078475A JP 2017078475 A JP2017078475 A JP 2017078475A JP 2015207135 A JP2015207135 A JP 2015207135A JP 2015207135 A JP2015207135 A JP 2015207135A JP 2017078475 A JP2017078475 A JP 2017078475A
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gas
medium
heat source
low
temperature liquefied
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JP6454628B2 (en
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正英 岩崎
Masahide Iwasaki
正英 岩崎
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Kobe Steel Ltd
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Kobe Steel Ltd
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Priority to JP2015207135A priority Critical patent/JP6454628B2/en
Priority to KR1020187013562A priority patent/KR102071985B1/en
Priority to CN201680061677.3A priority patent/CN108351072B/en
Priority to SG11201803070SA priority patent/SG11201803070SA/en
Priority to PCT/JP2016/079719 priority patent/WO2017068983A1/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C9/00Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
    • F17C9/02Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure with change of state, e.g. vaporisation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17DPIPE-LINE SYSTEMS; PIPE-LINES
    • F17D1/00Pipe-line systems
    • F17D1/02Pipe-line systems for gases or vapours
    • F17D1/04Pipe-line systems for gases or vapours for distribution of gas
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2205/00Vessel construction, in particular mounting arrangements, attachments or identifications means
    • F17C2205/03Fluid connections, filters, valves, closure means or other attachments
    • F17C2205/0302Fittings, valves, filters, or components in connection with the gas storage device
    • F17C2205/0323Valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03Heat exchange with the fluid
    • F17C2227/0302Heat exchange with the fluid by heating
    • F17C2227/0309Heat exchange with the fluid by heating using another fluid
    • F17C2227/0311Air heating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03Heat exchange with the fluid
    • F17C2227/0302Heat exchange with the fluid by heating
    • F17C2227/0309Heat exchange with the fluid by heating using another fluid
    • F17C2227/0316Water heating
    • F17C2227/0318Water heating using seawater

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Pipeline Systems (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an intermediate medium type gas vaporizer which enables reduction of a diameter of a housing of a warmer.SOLUTION: An intermediate medium type gas vaporizer includes: a housing part (10); an intermediate medium evaporation part (E1); a low temperature liquified gas vaporization part (E2); a housing (31); a gas heating part (E3); a first heat source medium supply passage (41); a second heat source medium supply passage (42); and a gas passage (50). The housing (31) includes: a trunk part (32); a first inflow part (32a) which is provided at one side end part of the trunk part (32); a second inflow part (32b) which is provided at the other side end part of the trunk part (32); and an outflow part (32c) provided at a portion of the trunk part (32) which is located between the one side end part and the other side end part. The gas passage (50) has: a first gas passage (50a) which supplies a part of a gas to the first inflow part (32a); and a second gas passage (50b) which supplies the other part of the gas to the second inflow part (32b).SELECTED DRAWING: Figure 1

Description

本発明は、中間媒体式ガス気化器に関するものである。   The present invention relates to an intermediate medium gas vaporizer.

従来、液化天然ガス(LNG)等の低温液化ガスを中間媒体(プロパン等)を用いて気化させる中間媒体式のガス気化器(IFV)が知られている。例えば、特許文献1には、中間媒体を収容するシェルと、中間媒体蒸発管と、伝熱管と、NG加温器と、NG導管と、熱源媒体供給管と、熱源媒体導管と、を備えるガス気化器が開示されている。   Conventionally, an intermediate-medium gas vaporizer (IFV) that vaporizes a low-temperature liquefied gas such as liquefied natural gas (LNG) using an intermediate medium (propane or the like) is known. For example, Patent Document 1 discloses a gas including a shell that stores an intermediate medium, an intermediate medium evaporation tube, a heat transfer tube, an NG heater, an NG conduit, a heat source medium supply tube, and a heat source medium conduit. A vaporizer is disclosed.

中間媒体蒸発管は、シェル内の下部に配置されている。中間媒体蒸発管内には、熱源媒体が供給される。中間媒体蒸発管は、当該中間媒体蒸発管内を流れる熱源媒体と液相の中間媒体とを熱交換させることによって中間媒体を蒸発させる。   The intermediate medium evaporator tube is disposed in the lower part of the shell. A heat source medium is supplied into the intermediate medium evaporation pipe. The intermediate medium evaporation pipe evaporates the intermediate medium by exchanging heat between the heat source medium flowing in the intermediate medium evaporation pipe and the liquid intermediate medium.

伝熱管は、シェル内の上部に配置されている。伝熱管内には、LNGが供給される。伝熱管は、当該伝熱管内を流れるLNGと気相の中間媒体とを熱交換させることによってLNGを気化させる。   The heat transfer tube is disposed at an upper portion in the shell. LNG is supplied into the heat transfer tube. The heat transfer tube vaporizes LNG by exchanging heat between the LNG flowing in the heat transfer tube and the gas phase intermediate medium.

NG加温器は、複数の熱源管と、これらの熱源管を収容する筐体と、を有している。各熱源管には、熱源媒体供給管を通じて熱源媒体が供給され、筐体内には、NG導管を通じて伝熱管から流出したNGが導かれる。筐体は、シェルから分離している。   The NG heater has a plurality of heat source tubes and a housing that accommodates these heat source tubes. A heat source medium is supplied to each heat source pipe through a heat source medium supply pipe, and NG that has flowed out of the heat transfer pipe is guided into the casing through an NG conduit. The housing is separated from the shell.

熱源媒体導管は、NG加温器の熱源管から流出した熱源媒体をシェル内の中間媒体蒸発管内に導く。つまり、熱源媒体は、熱源管及び中間媒体蒸発管をこの順に直列に流れる。   The heat source medium conduit guides the heat source medium flowing out from the heat source pipe of the NG warmer into the intermediate medium evaporation pipe in the shell. That is, the heat source medium flows in series in this order through the heat source pipe and the intermediate medium evaporation pipe.

特開2001−200995号公報JP 2001-200995 A

特許文献1に記載される中間媒体式ガス気化器では、NG加温器が大型化する。具体的に、熱源管においてNGを加熱するのに必要な熱量と、中間媒体蒸発管において液相の中間媒体を蒸発させるのに必要な熱量と、では、前者の方が小さいものの、上記中間媒体式ガス気化器では、熱源媒体が熱源管及び中間媒体蒸発管を直列に流れるので、熱源管には、中間媒体蒸発管への流量と同じ流量の熱源媒体が供給される。このため、加温器の熱源管の管数が多くなるので、筐体(NG加温器)が大径化する。   In the intermediate-medium gas vaporizer described in Patent Document 1, the NG heater is increased in size. Specifically, the amount of heat necessary for heating NG in the heat source tube and the amount of heat necessary for evaporating the liquid phase intermediate medium in the intermediate medium evaporation tube are smaller than the former, but the intermediate medium In the gas vaporizer, since the heat source medium flows in series through the heat source pipe and the intermediate medium evaporation pipe, the heat source medium is supplied with the same flow rate as the flow to the intermediate medium evaporation pipe. For this reason, since the number of heat source tubes of the warmer increases, the casing (NG warmer) has a large diameter.

本発明の目的は、筐体の小径化が可能な中間媒体式ガス気化器を提供することである。   An object of the present invention is to provide an intermediate-medium gas vaporizer capable of reducing the diameter of a casing.

前記課題を解決するために、熱源管(以下、「ガス加熱部」という)及び中間媒体蒸発管(以下、「中間媒体蒸発部」という)に対して並列に熱源媒体を供給すること、つまり、中間媒体蒸発部に熱源媒体を供給する第1熱源媒体供給流路と、ガス加熱部に熱源媒体を供給する第2熱源媒体供給流路と、を設けることが考えられる。このようにすれば、中間媒体蒸発部に必要な熱源媒体の流量とは独立してガス加熱部に供給する熱源媒体の流量を設定することが可能となる。これにより、ガス加熱部の熱源管の本数の低減が可能となるので、加温器の筐体の小径化が可能となる。ただし、筐体の小径化により、筐体内を流れるガスの流速が大きくなるので、当該ガスのエネルギーによってガス加熱部が振動する懸念がある。   In order to solve the above problems, supplying a heat source medium in parallel to a heat source pipe (hereinafter referred to as “gas heating section”) and an intermediate medium evaporation pipe (hereinafter referred to as “intermediate medium evaporation section”), that is, It is conceivable to provide a first heat source medium supply channel for supplying the heat source medium to the intermediate medium evaporation unit and a second heat source medium supply channel for supplying the heat source medium to the gas heating unit. In this way, it is possible to set the flow rate of the heat source medium supplied to the gas heating unit independently of the flow rate of the heat source medium required for the intermediate medium evaporation unit. As a result, the number of heat source tubes of the gas heating unit can be reduced, so that the diameter of the casing of the heater can be reduced. However, since the flow velocity of the gas flowing in the casing increases due to the reduction in the diameter of the casing, there is a concern that the gas heating unit vibrates due to the energy of the gas.

そこで、鋭意検討した結果、本発明者らは、前記エネルギーは、筐体の断面あたりのガスの流量の増減に伴い増減するので、この流量を減らすこと、つまり、低温液化ガス気化部から流出したガスの全量が一様に筐体内を流れるのではなく筐体内におけるガスの流路を分けることにより、ガス加熱部の振動を抑制可能であることに想到した。   Therefore, as a result of intensive studies, the present inventors increased or decreased the energy with the increase or decrease of the flow rate of gas per cross section of the casing, so that this flow rate was reduced, that is, the low temperature liquefied gas vaporization part flowed out. It was conceived that the vibration of the gas heating unit can be suppressed by dividing the gas flow path in the housing instead of the entire amount of gas flowing uniformly in the housing.

本発明は、このような観点からなされたものであり、低温液化ガスを当該低温液化ガスの沸点よりも高い沸点を有する中間媒体を用いて気化させる中間媒体式ガス気化器であって、前記中間媒体を収容する収容部と、前記収容部内に配置されており、熱源媒体が導入される中間媒体蒸発部と、前記収容部内に配置されており、前記低温液化ガスが導入される低温液化ガス気化部と、前記低温液化ガス気化部での前記低温液化ガスの気化により生じたガスが導入される筐体と、前記筐体内に配置されており、前記熱源媒体が導入されるガス加熱部と、前記中間媒体蒸発部へ前記熱源媒体を供給する第1熱源媒体供給流路と、前記ガス加熱部へ前記熱源媒体を供給する第2熱源媒体供給流路と、前記低温液化ガス気化部から流出したガスを前記筐体に導くガス流路と、を備え、前記中間媒体蒸発部は、当該中間媒体蒸発部内を流れる前記熱源媒体と当該中間媒体蒸発部外に存在する前記中間媒体とを熱交換させることによって前記中間媒体の少なくとも一部を蒸発させ、前記低温液化ガス気化部は、当該低温液化ガス気化部内を流れる前記低温液化ガスと当該低温液化ガス気化部外に存在する前記中間媒体とを熱交換させることによって前記低温液化ガスの少なくとも一部を気化させ、前記ガス加熱部は、当該ガス加熱部内を流れる前記熱源媒体と当該ガス加熱部外に存在する前記ガスとを熱交換させることによって前記ガスを加熱し、前記筐体は、前記ガス加熱部を収容する胴部と、前記胴部の一方側の端部に設けられており、前記ガスを前記胴部内に流入させる第1流入部と、前記胴部の他方側の端部に設けられており、前記ガスを前記胴部内に流入させる第2流入部と、前記胴部のうち前記一方側の端部と前記他方側の端部との間の部位に設けられており、前記ガスを前記胴部から流出させる流出部と、を有し、前記ガス流路は、前記低温液化ガス気化部から流出したガスの一部を前記第1流入部に供給する第1ガス流路と、前記低温液化ガス気化部から流出したガスの残部を前記第2流入部に供給する第2ガス流路と、を有する、中間媒体式ガス気化器を提供する。   The present invention has been made from such a viewpoint, and is an intermediate medium gas vaporizer that vaporizes a low-temperature liquefied gas using an intermediate medium having a boiling point higher than that of the low-temperature liquefied gas. A storage unit for storing a medium, an intermediate medium evaporation unit that is disposed in the storage unit and into which the heat source medium is introduced, and a low-temperature liquefied gas vaporization that is disposed in the storage unit and into which the low-temperature liquefied gas is introduced A casing in which gas generated by vaporization of the low-temperature liquefied gas in the low-temperature liquefied gas vaporization section, a gas heating section that is disposed in the casing and into which the heat source medium is introduced, The first heat source medium supply flow path for supplying the heat source medium to the intermediate medium evaporation section, the second heat source medium supply flow path for supplying the heat source medium to the gas heating section, and the low-temperature liquefied gas vaporization section Gas A gas flow path leading to the intermediate medium evaporating unit, wherein the intermediate medium evaporating unit exchanges heat between the heat source medium flowing in the intermediate medium evaporating unit and the intermediate medium existing outside the intermediate medium evaporating unit. The low-temperature liquefied gas vaporization section evaporates at least a part of Vaporizing at least part of the low-temperature liquefied gas, the gas heating unit heats the gas by causing heat exchange between the heat source medium flowing in the gas heating unit and the gas existing outside the gas heating unit; The casing is provided at a barrel portion that houses the gas heating portion, an end portion on one side of the barrel portion, a first inflow portion that allows the gas to flow into the barrel portion, Between the second inflow part for allowing the gas to flow into the body part, and the one side end part and the other side end part of the body part. And an outflow portion for allowing the gas to flow out of the body portion, and the gas flow path allows a part of the gas flowing out of the low-temperature liquefied gas vaporization portion to the first inflow portion. An intermediate medium type gas carburetor having a first gas flow path for supplying and a second gas flow path for supplying the remaining gas flowing out from the low-temperature liquefied gas vaporization section to the second inflow section is provided.

本中間媒体式ガス気化器では、第1熱源媒体供給流路及び第2熱源媒体供給流路によりガス加熱部及び中間媒体蒸発部に対して並列的に熱源媒体が供給されるので、筐体の小径化が可能となり、しかも、筐体内におけるガスの流路が分かれているので、ガス加熱部の振動が抑制される。具体的に、低温液化ガス気化部から流出したガスの一部は、第1ガス流路及び第1流入部から胴部内に流入してから流出部に向かう一方、前記ガスの残部は、第2ガス流路及び第2流入部から胴部内に流入してから流出部に向かうので、胴部の断面あたりのガスの流量が低減する。よって、ガス加熱部の振動が抑制される。   In this intermediate medium type gas vaporizer, the heat source medium is supplied in parallel to the gas heating unit and the intermediate medium evaporation unit through the first heat source medium supply channel and the second heat source medium supply channel. The diameter can be reduced, and the gas flow path in the housing is separated, so that vibration of the gas heating unit is suppressed. Specifically, a part of the gas flowing out from the low temperature liquefied gas vaporization part flows into the trunk part from the first gas flow path and the first inflow part and then goes to the outflow part, while the remaining part of the gas is the second Since the gas flow path and the second inflow portion flow into the body portion and then go to the outflow portion, the gas flow rate per cross section of the body portion is reduced. Therefore, the vibration of the gas heating unit is suppressed.

この場合において、前記熱源媒体を前記第1熱源媒体供給流路と前記第2熱源媒体供給流路とに供給する共通供給流路と、前記第1熱源媒体供給流路に設けられており、開度調整が可能な第1開閉弁と、前記第2熱源媒体供給流路に設けられており、開度調整が可能な第2開閉弁と、をさらに備え、各開閉弁の開度は、前記中間媒体蒸発部への前記熱源媒体の供給量の前記ガス加熱部への前記熱源媒体の供給量に対する供給割合が3以上5以下となるように設定されていることが好ましい。   In this case, the heat source medium is provided in the common heat supply channel for supplying the heat source medium to the first heat source medium supply flow channel and the second heat source medium supply flow channel, and the first heat source medium supply flow channel. A first opening / closing valve capable of adjusting the degree of opening, and a second opening / closing valve provided in the second heat source medium supply flow path, the opening degree of which can be adjusted. It is preferable that the supply ratio of the supply amount of the heat source medium to the intermediate medium evaporation unit to the supply amount of the heat source medium to the gas heating unit is set to 3 or more and 5 or less.

このようにすれば、筐体の小径化とガス加熱部の振動の抑止との双方が有効に達成される。   In this way, both reduction in the diameter of the housing and suppression of vibration of the gas heating unit can be effectively achieved.

さらにこの場合において、前記ガス加熱部から流出した熱源媒体を前記第1熱源媒体供給流路に合流させる熱源媒体合流流路をさらに備えることが好ましい。   Furthermore, in this case, it is preferable to further include a heat source medium merging channel for merging the heat source medium flowing out from the gas heating unit with the first heat source medium supply channel.

このようにすれば、中間媒体蒸発部への熱源媒体の供給量が確保されるので、前記供給割合の範囲内においてガス加熱部への熱源媒体の供給量を増やすことができる。これにより、ガス加熱部において熱源媒体がガスに与える熱量が増加するので、ガス加熱部の伝熱面積を小さくする等ガス加熱部の設計自由度が向上する。   In this way, since the supply amount of the heat source medium to the intermediate medium evaporation unit is ensured, the supply amount of the heat source medium to the gas heating unit can be increased within the range of the supply ratio. As a result, the amount of heat given to the gas by the heat source medium in the gas heating unit increases, so that the degree of freedom in designing the gas heating unit such as reducing the heat transfer area of the gas heating unit is improved.

また、前記中間媒体式ガス気化器において、前記胴部の長さの前記胴部の径に対する割合は、5以上10以下に設定されていることが好ましい。   In the intermediate medium gas vaporizer, the ratio of the length of the body portion to the diameter of the body portion is preferably set to 5 or more and 10 or less.

また、前記中間媒体式ガス気化器において、前記胴部の径の前記収容部の径に対する割合は、0.5以下に設定されていることが好ましい。   In the intermediate medium type gas vaporizer, the ratio of the diameter of the body portion to the diameter of the housing portion is preferably set to 0.5 or less.

また、前記中間媒体式ガス気化器において、前記収容部の長さの前記胴部の長さに対する割合は、1.3以下に設定されていることが好ましい。   In the intermediate medium type gas vaporizer, the ratio of the length of the housing portion to the length of the body portion is preferably set to 1.3 or less.

また、前記中間媒体式ガス気化器において、前記胴部の一方側の端部に接続され、前記ガス加熱部内と連通する入口室と、前記胴部の一方側の端部に接続され、前記ガス加熱部内と連通する出口室と、前記胴部の一方側の端部に接続され、前記入口室と前記出口室とを仕切る仕切壁と、前記胴部の他方側の端部に接続され、前記ガス加熱部内と連通する折り返し室と、をさらに備えてもよい。   Further, in the intermediate medium type gas vaporizer, connected to one end of the barrel, communicated with the inside of the gas heating unit, and connected to one end of the barrel, the gas An outlet chamber communicating with the inside of the heating unit, connected to one end of the barrel, a partition wall partitioning the inlet chamber and the outlet chamber, connected to the other end of the barrel, A folding chamber communicating with the inside of the gas heating unit may be further provided.

このようにすれば、ガス加熱部の長さが略半分となるので、加温器全体の長さが短縮される。   In this way, since the length of the gas heating part is substantially halved, the entire length of the heater is shortened.

また、本発明は、低温液化ガスを当該低温液化ガスの沸点よりも高い沸点を有する中間媒体を用いて気化させる中間媒体式ガス気化器であって、前記中間媒体を収容する収容部と、前記収容部内に配置されており、熱源媒体が導入される中間媒体蒸発部と、前記収容部内に配置されており、前記低温液化ガスが導入される低温液化ガス気化部と、前記収容部から分離しており、前記低温液化ガス気化部での前記低温液化ガスの気化により生じたガスが導入される筐体と、前記筐体内に配置されており、前記熱源媒体が導入されるガス加熱部と、前記中間媒体蒸発部へ前記熱源媒体を供給する第1熱源媒体供給流路と、前記ガス加熱部へ前記熱源媒体を供給する第2熱源媒体供給流路と、前記低温液化ガス気化部から流出したガスを前記筐体に導くガス流路と、を備え、前記中間媒体蒸発部は、当該中間媒体蒸発部内を流れる前記熱源媒体と当該中間媒体蒸発部外に存在する前記中間媒体とを熱交換させることによって前記中間媒体の少なくとも一部を蒸発させ、前記低温液化ガス気化部は、当該低温液化ガス気化部内を流れる前記低温液化ガスと当該低温液化ガス気化部外に存在する前記中間媒体とを熱交換させることによって前記低温液化ガスの少なくとも一部を気化させ、前記ガス加熱部は、当該ガス加熱部内を流れる前記熱源媒体と当該ガス加熱部外に存在する前記ガスとを熱交換させることによって前記ガスを加熱し、前記筐体は、前記ガス加熱部を収容する胴部と、前記胴部の一方側の端部に設けられており、前記ガスを前記胴部から流出させる第1流出部と、前記胴部の他方側の端部に設けられており、前記ガスを前記胴部から流出させる第2流出部と、前記胴部のうち前記一方側の端部と前記他方側の端部との間の部位に設けられており、前記ガスを前記胴部内に流入させる流入部と、を有し、前記ガス流路の下流側の端部は、前記流入部に接続されている、中間媒体式ガス気化器を提供する。   Further, the present invention is an intermediate medium type gas vaporizer for vaporizing a low-temperature liquefied gas using an intermediate medium having a boiling point higher than the boiling point of the low-temperature liquefied gas, containing the intermediate medium, An intermediate medium evaporation section that is disposed in the housing section and into which the heat source medium is introduced, a low-temperature liquefied gas vaporization section that is disposed in the housing section and into which the low-temperature liquefied gas is introduced, and is separated from the housing section. A casing into which gas generated by vaporization of the low-temperature liquefied gas in the low-temperature liquefied gas vaporization section, a gas heating section that is arranged in the casing and into which the heat source medium is introduced, The first heat source medium supply flow path for supplying the heat source medium to the intermediate medium evaporation section, the second heat source medium supply flow path for supplying the heat source medium to the gas heating section, and the low-temperature liquefied gas vaporization section Gas into the housing A gas flow path, wherein the intermediate medium evaporation section exchanges heat between the heat source medium flowing in the intermediate medium evaporation section and the intermediate medium existing outside the intermediate medium evaporation section. The low temperature liquefied gas vaporization unit evaporates at least a part, and the low temperature liquefied gas vaporization unit heat-exchanges the low temperature liquefied gas flowing in the low temperature liquefied gas vaporization unit and the intermediate medium existing outside the low temperature liquefied gas vaporization unit. Vaporizing at least part of the liquefied gas, the gas heating unit heats the gas by exchanging heat between the heat source medium flowing in the gas heating unit and the gas existing outside the gas heating unit, The casing is provided at a barrel portion that houses the gas heating unit, an end portion on one side of the barrel portion, a first outflow portion that allows the gas to flow out of the trunk portion, and the trunk portion A second outflow portion that is provided at an end portion on the other side and allows the gas to flow out from the body portion; and a portion between the end portion on the one side and the end portion on the other side of the body portion. An intermediate medium type gas carburetor provided at the downstream end of the gas flow path and connected to the inflow portion. provide.

本中間媒体式ガス気化器においても、筐体の小径化が可能となり、しかも、筐体内におけるガスの流路が分かれているので、ガス加熱部の振動が抑制される。   Also in this intermediate medium type gas vaporizer, the casing can be reduced in diameter, and the gas flow path in the casing is separated, so that the vibration of the gas heating unit is suppressed.

以上のように、本発明によれば、筐体の小径化が可能でかつガス加熱部の振動を抑制可能な中間媒体式ガス気化器を提供することができる。   As described above, according to the present invention, it is possible to provide an intermediate-medium gas vaporizer capable of reducing the diameter of the housing and suppressing the vibration of the gas heating unit.

本発明の一実施形態の中間媒体式ガス気化器の構成の概略を示す図である。It is a figure which shows the outline of a structure of the intermediate | middle medium type gas vaporizer of one Embodiment of this invention. 図1に示される中間媒体式ガス気化器の平面図である。It is a top view of the intermediate | middle medium type gas vaporizer shown by FIG. 図1に示される中間媒体式ガス気化器の変形例を示す図である。It is a figure which shows the modification of the intermediate | middle medium type gas vaporizer shown by FIG. 収容部と筐体との配置関係の変形例を示す図である。It is a figure which shows the modification of the arrangement | positioning relationship between an accommodating part and a housing | casing. 加温器の変形例を示す図である。It is a figure which shows the modification of a warmer.

本発明の一実施形態の中間媒体式ガス気化器1について、図1〜図2を参照しながら説明する。中間媒体式ガス気化器1は、低温液化ガスを当該低温液化ガスの沸点よりも高い沸点を有する中間媒体を用いて気化させる中間媒体式ガス気化器(IFV)である。本実施形態では、低温液化ガスとして液化天然ガス(LNG)が用いられ、中間媒体としてプロパンが用いられている。ただし、低温液化ガスは、エチレン、液化酸素、液化窒素等であってもよい。また、中間媒体は、プロパンに限られない。この中間媒体式ガス気化器1では、中間媒体の加熱は、熱源媒体(海水や大気等)により行われる。   An intermediate medium type gas vaporizer 1 according to an embodiment of the present invention will be described with reference to FIGS. The intermediate medium gas vaporizer 1 is an intermediate medium gas vaporizer (IFV) that vaporizes a low-temperature liquefied gas using an intermediate medium having a boiling point higher than that of the low-temperature liquefied gas. In the present embodiment, liquefied natural gas (LNG) is used as the low-temperature liquefied gas, and propane is used as the intermediate medium. However, the low temperature liquefied gas may be ethylene, liquefied oxygen, liquefied nitrogen or the like. Further, the intermediate medium is not limited to propane. In the intermediate medium gas vaporizer 1, the intermediate medium is heated by a heat source medium (seawater, air, etc.).

図1に示されるように、中間媒体式ガス気化器1は、中間媒体2と、中間媒体2を収容する収容部10と、中間媒体蒸発部E1と、低温液化ガス気化部E2と、加温器30と、第1熱源媒体供給流路41と、第2熱源媒体供給流路42と、ガス流路50と、を備えている。   As shown in FIG. 1, the intermediate medium type gas vaporizer 1 includes an intermediate medium 2, a storage unit 10 that stores the intermediate medium 2, an intermediate medium evaporation unit E <b> 1, a low-temperature liquefied gas vaporization unit E <b> 2, and heating. A heat source medium supply channel 41, a second heat source medium supply channel 42, and a gas channel 50.

収容部10は、中間媒体2、中間媒体蒸発部E1及び低温液化ガス気化部E2をまとめて収容する単一のケーシングにより形成されている。収容部10は、円筒状に形成されている。   The accommodating part 10 is formed of a single casing that collectively accommodates the intermediate medium 2, the intermediate medium evaporating part E1, and the low-temperature liquefied gas vaporizing part E2. The accommodating part 10 is formed in a cylindrical shape.

中間媒体蒸発部E1は、収容部10内に配置されている。より具体的には、中間媒体蒸発部E1は、収容部10内の下部(液相の中間媒体2に浸る位置)に配置されている。中間媒体蒸発部E1は、複数の伝熱管の束により構成されている。中間媒体蒸発部E1内に熱源媒体が導入される。中間媒体蒸発部E1は、当該中間媒体蒸発部E1内を流れる熱源媒体と収容部10内の下部に存在する液相の中間媒体2とを熱交換させることによって中間媒体2の少なくとも一部を蒸発させる。   The intermediate medium evaporating unit E1 is disposed in the accommodating unit 10. More specifically, the intermediate medium evaporating unit E1 is disposed in a lower part (a position where the intermediate medium 2 in the liquid phase is immersed) in the housing unit 10. The intermediate medium evaporation part E1 is configured by a bundle of a plurality of heat transfer tubes. A heat source medium is introduced into the intermediate medium evaporation section E1. The intermediate medium evaporating unit E1 evaporates at least a part of the intermediate medium 2 by exchanging heat between the heat source medium flowing in the intermediate medium evaporating unit E1 and the liquid intermediate medium 2 existing in the lower part of the storage unit 10. Let

低温液化ガス気化部E2は、収容部10内に配置されている。より具体的には、低温液化ガス気化部E2は、収容部10内の上部(気相の中間媒体2が存在する領域)に配置されている。本実施形態では、低温液化ガス気化部E2は、U字状に形成された伝熱管により構成されている。低温液化ガス気化部E2内に低温液化ガスが導入される。低温液化ガス気化部E2は、当該低温液化ガス気化部E2内を流れる低温液化ガスと収容部10内の気相の中間媒体2とを熱交換させることによって当該低温液化ガスの少なくとも一部を気化させる。   The low-temperature liquefied gas vaporization part E <b> 2 is disposed in the housing part 10. More specifically, the low temperature liquefied gas vaporization part E2 is arrange | positioned in the upper part in the accommodating part 10 (area | region where the gaseous-phase intermediate medium 2 exists). In this embodiment, the low temperature liquefied gas vaporization part E2 is comprised by the heat exchanger tube formed in the U-shape. A low-temperature liquefied gas is introduced into the low-temperature liquefied gas vaporization section E2. The low-temperature liquefied gas vaporization section E2 vaporizes at least a part of the low-temperature liquefied gas by exchanging heat between the low-temperature liquefied gas flowing in the low-temperature liquefied gas vaporization section E2 and the gas phase intermediate medium 2 in the storage section 10. Let

収容部10の一方側の端部の下部には、互いに仕切板20で仕切られた入口室21及び出口室22が接続されている。入口室21及び出口室22は、それぞれ中間媒体蒸発部E1内と連通している。収容部10の他方側の端部の下部には、折り返し室23が接続されている。折り返し室23は、中間媒体蒸発部E1内と連通している。すなわち、中間媒体蒸発部E1は、いわゆる2パス方式である。   An inlet chamber 21 and an outlet chamber 22 that are partitioned by a partition plate 20 are connected to a lower portion of one end portion of the accommodating portion 10. The inlet chamber 21 and the outlet chamber 22 communicate with the intermediate medium evaporator E1. A folding chamber 23 is connected to the lower part of the other end of the housing part 10. The folding chamber 23 communicates with the inside of the intermediate medium evaporator E1. That is, the intermediate medium evaporation unit E1 is a so-called two-pass method.

収容部10の上部には、互いに仕切板24で仕切られた入口室25及び出口室26が接続されている。低温液化ガス気化部E2の一端は、低温液化ガス気化部E2内と入口室25内とが連通するように入口室25に接続されている。低温液化ガス気化部E2の他端は、低温液化ガス気化部E2内と出口室26内とが連通するように出口室26に接続されている。   An inlet chamber 25 and an outlet chamber 26 that are partitioned by a partition plate 24 are connected to the upper portion of the accommodating portion 10. One end of the low-temperature liquefied gas vaporization section E2 is connected to the inlet chamber 25 so that the inside of the low-temperature liquefied gas vaporization section E2 and the inside of the inlet chamber 25 communicate with each other. The other end of the low temperature liquefied gas vaporization part E2 is connected to the outlet chamber 26 so that the inside of the low temperature liquefied gas vaporization part E2 and the inside of the outlet chamber 26 communicate.

加温器30は、低温液化ガスの気化により生じたガスを加熱する。加温器30は、熱源媒体が導入されるガス加熱部E3と、ガス加熱部E3を収容する筐体31と、を有している。   The warmer 30 heats the gas generated by the vaporization of the low-temperature liquefied gas. The warmer 30 includes a gas heating unit E3 into which a heat source medium is introduced, and a housing 31 that houses the gas heating unit E3.

ガス加熱部E3は、複数の伝熱管の束により構成されている。ガス加熱部E3は、当該ガス加熱部E3内を流れる熱源媒体と筐体31内に供給されたガスとを熱交換させることによってガスを加熱する。   The gas heating unit E3 is configured by a bundle of a plurality of heat transfer tubes. The gas heating unit E3 heats the gas by exchanging heat between the heat source medium flowing in the gas heating unit E3 and the gas supplied into the housing 31.

筐体31は、胴部32と、第1流入部32aと、第2流入部32bと、流出部32cと、を有している。   The housing 31 includes a body portion 32, a first inflow portion 32a, a second inflow portion 32b, and an outflow portion 32c.

胴部32は、ガス加熱部E3を収容可能な円筒状に形成されている。第1流入部32aは、胴部32の一方側の端部に設けられており、ガスを胴部32内に流入させる。第2流入部32bは、胴部32の他方側の端部に設けられており、ガスを胴部32内に流入させる。流出部32cは、胴部32のうち一方側の端部と他方側の端部との間の部位に設けられており、ガスを胴部32から流出させる。   The trunk | drum 32 is formed in the cylindrical shape which can accommodate the gas heating part E3. The first inflow portion 32 a is provided at an end portion on one side of the body portion 32 and allows gas to flow into the body portion 32. The second inflow portion 32 b is provided at the other end portion of the body portion 32 and allows gas to flow into the body portion 32. The outflow portion 32 c is provided in a portion between the end portion on one side and the end portion on the other side of the body portion 32, and allows gas to flow out from the body portion 32.

胴部32の一方側の端部には、互いに仕切板35で仕切られた入口室36及び出口室37が接続されている。入口室36及び出口室37は、それぞれガス加熱部E3内と連通している。胴部32の他方側の端部には、折り返し室38が接続されている。折り返し室38は、ガス加熱部E3内と連通している。すなわち、ガス加熱部E3は、いわゆる2パス方式である。   An inlet chamber 36 and an outlet chamber 37 that are partitioned by a partition plate 35 are connected to one end portion of the body portion 32. The inlet chamber 36 and the outlet chamber 37 communicate with the inside of the gas heating unit E3. A folding chamber 38 is connected to the other end portion of the body portion 32. The folding chamber 38 communicates with the gas heating unit E3. That is, the gas heating unit E3 is a so-called two-pass method.

図2に示されるように、加温器30は、収容部10の上部に載置される。本実施形態では、胴部32の長さL3の胴部32の径D3に対する割合L3/D3は、5以上10以下に設定されている。胴部32の径D3の収容部10の径D1に対する割合D3/D1は、0.5以下に設定されている。収容部10の長さL1の胴部32の長さL3に対する割合L1/L3は、0.8以上1.3以下に設定されている。   As shown in FIG. 2, the warmer 30 is placed on the upper portion of the housing unit 10. In the present embodiment, the ratio L3 / D3 of the length L3 of the body portion 32 to the diameter D3 of the body portion 32 is set to 5 or more and 10 or less. A ratio D3 / D1 of the diameter D3 of the trunk portion 32 to the diameter D1 of the accommodating portion 10 is set to 0.5 or less. A ratio L1 / L3 of the length L1 of the accommodating portion 10 to the length L3 of the trunk portion 32 is set to 0.8 or more and 1.3 or less.

第1熱源媒体供給流路41は、中間媒体蒸発部E1へ熱源媒体を供給する流路である。第1熱源媒体供給流路41は、収容部10に接続された入口室21に接続されている。第1熱源媒体供給流路41には、開度調整が可能な第1開閉弁V1が設けられている。   The first heat source medium supply channel 41 is a channel for supplying the heat source medium to the intermediate medium evaporation unit E1. The first heat source medium supply channel 41 is connected to the inlet chamber 21 connected to the housing unit 10. The first heat source medium supply channel 41 is provided with a first on-off valve V1 whose opening degree can be adjusted.

第2熱源媒体供給流路42は、ガス加熱部E3へ熱源媒体を供給する流路である。第2熱源媒体供給流路42は、胴部32に接続された入口室36に接続されている。第2熱源媒体供給流路42には、開度調整が可能な第2開閉弁V2が設けられている。   The second heat source medium supply channel 42 is a channel for supplying the heat source medium to the gas heating unit E3. The second heat source medium supply flow path 42 is connected to an inlet chamber 36 connected to the trunk portion 32. The second heat source medium supply channel 42 is provided with a second on-off valve V2 capable of adjusting the opening degree.

本実施形態では、共通供給流路40と、熱源媒体合流流路43と、をさらに備えている。   In the present embodiment, a common supply channel 40 and a heat source medium merging channel 43 are further provided.

共通供給流路40は、第1熱源媒体供給流路41と第2熱源媒体供給流路42とに熱源媒体を供給する流路である。共通供給流路40には、熱源媒体の流量を調整可能な流量調整部(開閉弁、流量計等)が設けられている。各開閉弁V1,V2の開度は、共通供給流路40から第1熱源媒体供給流路41へ分岐した熱源媒体の流量と熱源媒体合流流路43を通じて第1熱源媒体供給流路41に合流した熱源媒体の流量とをあわせた量の、共通供給流路40から第2熱源媒体供給流路42へ分岐した熱源媒体の流量に対する割合、すなわち、中間媒体蒸発部E1への熱源媒体の供給量のガス加熱部E3への熱源媒体の供給量に対する供給割合が、3以上5以下となるように設定されている。   The common supply channel 40 is a channel that supplies the heat source medium to the first heat source medium supply channel 41 and the second heat source medium supply channel 42. The common supply channel 40 is provided with a flow rate adjusting unit (an on-off valve, a flow meter, etc.) that can adjust the flow rate of the heat source medium. The opening degree of each on-off valve V1, V2 is merged with the first heat source medium supply channel 41 through the heat source medium flow rate branched from the common supply channel 40 to the first heat source medium supply channel 41 and the heat source medium merge channel 43. The ratio of the combined amount of the heat source medium to the flow rate of the heat source medium branched from the common supply channel 40 to the second heat source medium supply channel 42, that is, the supply amount of the heat source medium to the intermediate medium evaporation unit E1 The supply ratio with respect to the supply amount of the heat source medium to the gas heating unit E3 is set to be 3 or more and 5 or less.

なお、各開閉弁V1,V2は、予め開度が設定されており取替可能な制限オリフィスであってもよい。   Each of the on-off valves V1, V2 may be a restrictive orifice that has a preset opening degree and can be replaced.

熱源媒体合流流路43は、ガス加熱部E3から流出した熱源媒体を第1熱源媒体供給流路41に合流させる流路である。具体的に、熱源媒体合流流路43の上流側の端部は、胴部32に接続された出口室37に接続されている。熱源媒体合流流路43の下流側の端部は、第1熱源媒体供給流路41のうち第1開閉弁V1と入口室21との間の部位に接続されている。なお、熱源媒体合流流路43の下流側の端部は、直接入口室21に接続されてもよい。   The heat source medium merge channel 43 is a channel that merges the heat source medium flowing out from the gas heating unit E3 with the first heat source medium supply channel 41. Specifically, the upstream end of the heat source medium merging flow path 43 is connected to an outlet chamber 37 connected to the body 32. The downstream end of the heat source medium merge channel 43 is connected to a portion of the first heat source medium supply channel 41 between the first on-off valve V1 and the inlet chamber 21. The downstream end of the heat source medium merge channel 43 may be directly connected to the inlet chamber 21.

ガス流路50は、低温液化ガス気化部E2から流出したガスを筐体31に導く流路である。ガス流路50の上流側の端部は、収容部10に接続された出口室26に接続されている。本実施形態では、ガス流路50の下流側の部位は、二股に分岐している。具体的に、ガス流路50は、低温液化ガス気化部E2から流出したガスの一部(本実施形態では、半分)を第1流入部32aに供給する第1ガス流路50aと、低温液化ガス気化部E2から流出したガスの残部を第2流入部32bに供給する第2ガス流路50bと、を有している。第1ガス流路50aの下流側の端部は、第1流入部32aに接続されており、第2ガス流路50bの下流側の端部は、第2流入部32bに接続されている。   The gas flow path 50 is a flow path that guides the gas flowing out from the low-temperature liquefied gas vaporization section E2 to the housing 31. The upstream end portion of the gas flow path 50 is connected to the outlet chamber 26 connected to the accommodating portion 10. In the present embodiment, the downstream portion of the gas flow path 50 is bifurcated. Specifically, the gas flow path 50 includes a first gas flow path 50a that supplies a part (half in this embodiment) of the gas flowing out from the low temperature liquefied gas vaporization section E2 to the first inflow section 32a, and a low temperature liquefaction. A second gas flow path 50b for supplying the remaining gas flowing out from the gas vaporization section E2 to the second inflow section 32b. The downstream end of the first gas passage 50a is connected to the first inflow portion 32a, and the downstream end of the second gas passage 50b is connected to the second inflow portion 32b.

中間媒体式ガス気化器1が駆動されると、第1熱源媒体供給流路41を通じて入口室21に熱源媒体が供給されるとともに第2熱源媒体供給流路42を通じて入口室36に熱源媒体が供給される一方、入口室25にLNGが供給される。   When the intermediate medium gas vaporizer 1 is driven, the heat source medium is supplied to the inlet chamber 21 through the first heat source medium supply flow path 41 and the heat source medium is supplied to the inlet chamber 36 through the second heat source medium supply flow path 42. On the other hand, LNG is supplied to the inlet chamber 25.

入口室21に供給された熱源媒体は、中間媒体蒸発部E1、折り返し室23、中間媒体蒸発部E1、出口室22をこの順に流れた後、外部に排出される。このとき、熱源媒体は、中間媒体蒸発部E1において、液相の中間媒体2を加熱し、これにより中間媒体2の少なくとも一部が蒸発する。入口室36に供給された熱源媒体は、ガス加熱部E3、折り返し室38、ガス加熱部E3、出口室37をこの順に流れた後、熱源媒体合流流路43を通じて第1熱源媒体供給流路41に合流する。このとき、熱源媒体は、ガス加熱部E3において、ガス(NG)を加熱する。   The heat source medium supplied to the inlet chamber 21 flows through the intermediate medium evaporator E1, the folding chamber 23, the intermediate medium evaporator E1, and the outlet chamber 22 in this order, and then is discharged to the outside. At this time, the heat source medium heats the liquid-phase intermediate medium 2 in the intermediate medium evaporation section E1, whereby at least a part of the intermediate medium 2 evaporates. The heat source medium supplied to the inlet chamber 36 flows through the gas heating unit E3, the folding chamber 38, the gas heating unit E3, and the outlet chamber 37 in this order, and then the first heat source medium supply channel 41 through the heat source medium merge channel 43. To join. At this time, the heat source medium heats the gas (NG) in the gas heating unit E3.

一方、入口室25に供給されたLNGは、低温液化ガス気化部E2内を通過する過程で収容部10内において気相の中間媒体2から熱を受けることによって気化する。低温液化ガス気化部E2から流出した低温のNGは、出口室26及びガス流路50を経由して筐体31内に流入する。具体的に、出口室26から流出した低温のNGの50%は、第1ガス流路50a及び第1流入部32aを介して胴部32内に流入し、出口室26から流出した低温のNGの残りの50%は、第2ガス流路50b及び第2流入部32bを介して胴部32内に流入する。第1流入部32aから胴部32内に流入した低温のNG及び第2流入部32bから胴部32内に流入した低温のNGは、それぞれ、流出部32cに向かう過程でガス加熱部E3内を流れる熱源媒体により加熱された後、流出部32cから常温のNGとなって流出する。   On the other hand, the LNG supplied to the inlet chamber 25 is vaporized by receiving heat from the vapor phase intermediate medium 2 in the accommodating portion 10 in the process of passing through the low temperature liquefied gas vaporizing portion E2. The low-temperature NG that has flowed out of the low-temperature liquefied gas vaporization section E <b> 2 flows into the housing 31 through the outlet chamber 26 and the gas flow path 50. Specifically, 50% of the low temperature NG flowing out from the outlet chamber 26 flows into the body portion 32 via the first gas flow path 50a and the first inflow portion 32a and flows out from the outlet chamber 26. The remaining 50% flows into the body portion 32 via the second gas flow path 50b and the second inflow portion 32b. The low-temperature NG that has flowed into the body portion 32 from the first inflow portion 32a and the low-temperature NG that has flowed into the body portion 32 from the second inflow portion 32b respectively travel through the gas heating portion E3 in the process toward the outflow portion 32c. After being heated by the flowing heat source medium, it flows out as NG at room temperature from the outflow part 32c.

以上に説明したように、本中間媒体式ガス気化器1では、第1熱源媒体供給流路41及び第2熱源媒体供給流路42によりガス加熱部E3及び中間媒体蒸発部E1に対して並列的に熱源媒体が供給されるので、筐体31の小径化が可能となり、しかも、筐体31内におけるガスの流路が分かれているので、ガス加熱部E3の振動が抑制される。具体的に、低温液化ガス気化部E2から流出したガスの約半分は、第1ガス流路50a及び第1流入部32aから胴部32内に流入してから流出部32cに向かう一方、前記ガスの残りの約半分は、第2ガス流路50b及び第2流入部32bから胴部内に流入してから流出部に向かうので、胴部32の断面あたりのガスの流量が低減する。よって、低温液化ガス気化部E2から流出したガスの全量が一様に胴部32内を流れる場合に比べ、胴部32内を流れるガスのエネルギーが約4分の1となるので、ガス加熱部E3の振動が抑制される。   As described above, in the intermediate medium type gas vaporizer 1, the first heat source medium supply channel 41 and the second heat source medium supply channel 42 are connected in parallel to the gas heating unit E3 and the intermediate medium evaporation unit E1. Since the heat source medium is supplied to the casing 31, the casing 31 can be reduced in diameter, and the gas flow path in the casing 31 is separated, so that the vibration of the gas heating section E3 is suppressed. Specifically, about half of the gas flowing out from the low temperature liquefied gas vaporization section E2 flows into the trunk section 32 from the first gas flow path 50a and the first inflow section 32a and then goes to the outflow section 32c. The remaining half of the gas flows from the second gas flow path 50b and the second inflow portion 32b into the trunk portion and then toward the outflow portion, so that the gas flow rate per cross section of the trunk portion 32 is reduced. Therefore, the energy of the gas flowing in the body 32 is about one-fourth that in the case where the entire amount of the gas flowing out from the low temperature liquefied gas vaporization section E2 flows in the body 32, so that the gas heating unit The vibration of E3 is suppressed.

そして、ガス加熱部E3及び中間媒体蒸発部E1に対して並列的に熱源媒体が供給されることにより、ガス加熱部E3を構成する伝熱管の数が低減されるので、伝熱管の溶接箇所や管板の厚みの低減に起因して製造コストが大幅に削減される。   Since the number of heat transfer tubes constituting the gas heating unit E3 is reduced by supplying the heat source medium in parallel to the gas heating unit E3 and the intermediate medium evaporation unit E1, Manufacturing costs are greatly reduced due to the reduced thickness of the tube sheet.

また、本実施形態では、各開閉弁V1,V2の開度は、前記供給割合が3以上5以下となるように設定されているので、筐体31の小径化とガス加熱部E3の振動の抑止との双方が有効に達成される。   In the present embodiment, the opening degree of each on-off valve V1, V2 is set so that the supply ratio is 3 or more and 5 or less, so that the diameter of the casing 31 is reduced and the vibration of the gas heating unit E3 is reduced. Both deterrence is effectively achieved.

また、本実施形態では、熱源媒体合流流路43を有しているので、中間媒体蒸発部E1への熱源媒体の供給量が確保される。このため、前記供給割合の範囲内においてガス加熱部E3への熱源媒体の供給量を増やすことができる。これにより、ガス加熱部E3において熱源媒体がガスに与える熱量が増加するので、ガス加熱部E3の伝熱面積を小さくする等ガス加熱部E3の設計自由度が向上する。   In the present embodiment, since the heat source medium merging flow path 43 is provided, the supply amount of the heat source medium to the intermediate medium evaporation unit E1 is ensured. For this reason, the supply amount of the heat source medium to the gas heating unit E3 can be increased within the range of the supply ratio. As a result, the amount of heat given to the gas by the heat source medium in the gas heating unit E3 increases, so that the degree of freedom in designing the gas heating unit E3 such as reducing the heat transfer area of the gas heating unit E3 is improved.

なお、今回開示された実施形態は、すべての点で例示であって制限的なものではないと考えられるべきである。本発明の範囲は、上記した実施形態の説明ではなく特許請求の範囲によって示され、さらに特許請求の範囲と均等の意味および範囲内でのすべての変更が含まれる。   The embodiment disclosed this time should be considered as illustrative in all points and not restrictive. The scope of the present invention is shown not by the above description of the embodiments but by the scope of claims for patent, and further includes all modifications within the meaning and scope equivalent to the scope of claims for patent.

例えば、図3に示されるように、胴部32の一方側の端部に入口室36aが接続され、胴部32の他方側の端部に出口室37aが接続されてもよい。つまり、ガス加熱部E3は、いわゆる1パス方式とされてもよい。このことは、中間媒体蒸発部E1についても同様である。   For example, as shown in FIG. 3, the inlet chamber 36 a may be connected to one end portion of the trunk portion 32, and the outlet chamber 37 a may be connected to the other end portion of the trunk portion 32. That is, the gas heating unit E3 may be a so-called one-pass method. The same applies to the intermediate medium evaporation unit E1.

また、図4に示されるように、加温器30は、収容部10の側方に載置されてもよい。   Further, as shown in FIG. 4, the warmer 30 may be placed on the side of the housing unit 10.

また、図5に示されるように、筐体31は、胴部32と、胴部32の一方側の端部に設けられた第1流出部32dと、胴部32の他方側の端部に設けられた第2流出部32eと、胴部32のうち一方側の端部と他方側の端部との間の部位に設けられた流入部32fと、を有していてもよい。この場合、ガス流路50の下流側の部位は、二股に分岐することなく流入部32fに接続される。   Further, as shown in FIG. 5, the casing 31 includes a trunk portion 32, a first outflow portion 32 d provided at one end portion of the trunk portion 32, and an end portion on the other side of the trunk portion 32. You may have the 2nd outflow part 32e provided, and the inflow part 32f provided in the site | part between the edge part of one side among the trunk | drum 32, and the edge part of the other side. In this case, the downstream portion of the gas flow path 50 is connected to the inflow portion 32f without branching into two branches.

1 中間媒体式ガス気化器
2 中間媒体
10 収容部
30 加温器
31 筐体
32 胴部
32a 第1流入部
32b 第2流入部
32c 流出部
35 仕切壁
36 入口室
37 出口室
38 折り返し室
40 共通供給流路
41 第1熱源媒体供給流路
42 第2熱源媒体供給流路
43 熱源媒体合流流路
50 ガス流路
50a 第1ガス流路
50b 第2ガス流路
E1 中間媒体蒸発部
E2 低温液化ガス気化部
E3 ガス加熱部
V1 第1開閉弁
V2 第2開閉弁
DESCRIPTION OF SYMBOLS 1 Intermediate | middle medium type gas vaporizer 2 Intermediate | middle medium 10 Accommodating part 30 Heater 31 Case 32 Trunk part 32a 1st inflow part 32b 2nd inflow part 32c Outflow part 35 Partition wall 36 Inlet room 37 Outlet room 38 Folding room 40 Common Supply flow path 41 First heat source medium supply flow path 42 Second heat source medium supply flow path 43 Heat source medium merge flow path 50 Gas flow path 50a First gas flow path 50b Second gas flow path E1 Intermediate medium evaporation section E2 Low temperature liquefied gas Vaporization part E3 Gas heating part V1 1st on-off valve V2 2nd on-off valve

Claims (8)

低温液化ガスを当該低温液化ガスの沸点よりも高い沸点を有する中間媒体を用いて気化させる中間媒体式ガス気化器であって、
前記中間媒体を収容する収容部と、
前記収容部内に配置されており、熱源媒体が導入される中間媒体蒸発部と、
前記収容部内に配置されており、前記低温液化ガスが導入される低温液化ガス気化部と、
前記低温液化ガス気化部での前記低温液化ガスの気化により生じたガスが導入される筐体と、
前記筐体内に配置されており、前記熱源媒体が導入されるガス加熱部と、
前記中間媒体蒸発部へ前記熱源媒体を供給する第1熱源媒体供給流路と、
前記ガス加熱部へ前記熱源媒体を供給する第2熱源媒体供給流路と、
前記低温液化ガス気化部から流出したガスを前記筐体に導くガス流路と、を備え、
前記中間媒体蒸発部は、当該中間媒体蒸発部内を流れる前記熱源媒体と当該中間媒体蒸発部外に存在する前記中間媒体とを熱交換させることによって前記中間媒体の少なくとも一部を蒸発させ、
前記低温液化ガス気化部は、当該低温液化ガス気化部内を流れる前記低温液化ガスと当該低温液化ガス気化部外に存在する前記中間媒体とを熱交換させることによって前記低温液化ガスの少なくとも一部を気化させ、
前記ガス加熱部は、当該ガス加熱部内を流れる前記熱源媒体と当該ガス加熱部外に存在する前記ガスとを熱交換させることによって前記ガスを加熱し、
前記筐体は、
前記ガス加熱部を収容する胴部と、
前記胴部の一方側の端部に設けられており、前記ガスを前記胴部内に流入させる第1流入部と、
前記胴部の他方側の端部に設けられており、前記ガスを前記胴部内に流入させる第2流入部と、
前記胴部のうち前記一方側の端部と前記他方側の端部との間の部位に設けられており、前記ガスを前記胴部から流出させる流出部と、を有し、
前記ガス流路は、
前記低温液化ガス気化部から流出したガスの一部を前記第1流入部に供給する第1ガス流路と、
前記低温液化ガス気化部から流出したガスの残部を前記第2流入部に供給する第2ガス流路と、を有する、中間媒体式ガス気化器。
An intermediate-medium gas vaporizer that vaporizes a low-temperature liquefied gas using an intermediate medium having a boiling point higher than that of the low-temperature liquefied gas,
An accommodating portion for accommodating the intermediate medium;
An intermediate medium evaporation section that is disposed in the housing section and into which the heat source medium is introduced;
A low-temperature liquefied gas vaporization section, which is disposed in the housing section and into which the low-temperature liquefied gas is introduced;
A casing into which gas generated by vaporization of the low-temperature liquefied gas in the low-temperature liquefied gas vaporization unit is introduced;
A gas heating unit disposed in the housing and into which the heat source medium is introduced;
A first heat source medium supply flow path for supplying the heat source medium to the intermediate medium evaporation section;
A second heat source medium supply channel for supplying the heat source medium to the gas heating unit;
A gas flow path for guiding the gas flowing out from the low-temperature liquefied gas vaporization section to the housing,
The intermediate medium evaporation section evaporates at least a part of the intermediate medium by exchanging heat between the heat source medium flowing in the intermediate medium evaporation section and the intermediate medium existing outside the intermediate medium evaporation section,
The low-temperature liquefied gas vaporization unit exchanges heat between the low-temperature liquefied gas flowing in the low-temperature liquefied gas vaporization unit and the intermediate medium existing outside the low-temperature liquefied gas vaporization unit, thereby at least part of the low-temperature liquefied gas Vaporize,
The gas heating unit heats the gas by exchanging heat between the heat source medium flowing in the gas heating unit and the gas existing outside the gas heating unit,
The housing is
A body portion for accommodating the gas heating unit;
A first inflow portion that is provided at an end portion on one side of the body portion and allows the gas to flow into the body portion;
A second inflow portion that is provided at an end portion on the other side of the body portion and allows the gas to flow into the body portion;
An outflow portion that is provided at a portion between the end portion on the one side and the end portion on the other side of the body portion, and causes the gas to flow out from the body portion;
The gas flow path is
A first gas flow path for supplying a part of the gas flowing out from the low-temperature liquefied gas vaporization section to the first inflow section;
An intermediate medium type gas vaporizer, comprising: a second gas flow path for supplying the remaining part of the gas flowing out from the low-temperature liquefied gas vaporization section to the second inflow section.
請求項1に記載の中間媒体式ガス気化器において、
前記熱源媒体を前記第1熱源媒体供給流路と前記第2熱源媒体供給流路とに供給する共通供給流路と、
前記第1熱源媒体供給流路に設けられており、開度調整が可能な第1開閉弁と、
前記第2熱源媒体供給流路に設けられており、開度調整が可能な第2開閉弁と、をさらに備え、
各開閉弁の開度は、前記中間媒体蒸発部への前記熱源媒体の供給量の前記ガス加熱部への前記熱源媒体の供給量に対する供給割合が3以上5以下となるように設定されている、中間媒体式ガス気化器。
The intermediate medium gas vaporizer according to claim 1,
A common supply channel for supplying the heat source medium to the first heat source medium supply channel and the second heat source medium supply channel;
A first on-off valve provided in the first heat source medium supply flow path and capable of adjusting an opening;
A second on-off valve provided in the second heat source medium supply flow path and capable of adjusting an opening;
The opening degree of each on-off valve is set such that the supply ratio of the supply amount of the heat source medium to the intermediate medium evaporation section to the supply amount of the heat source medium to the gas heating section is 3 or more and 5 or less. Intermediate medium gas vaporizer.
請求項2に記載の中間媒体式ガス気化器において、
前記ガス加熱部から流出した熱源媒体を前記第1熱源媒体供給流路に合流させる熱源媒体合流流路をさらに備える、中間媒体式ガス気化器。
The intermediate medium gas vaporizer according to claim 2,
An intermediate-medium gas vaporizer further comprising a heat source medium merging channel that merges the heat source medium flowing out from the gas heating unit into the first heat source medium supply channel.
請求項1ないし3のいずれかに記載の中間媒体式ガス気化器において、
前記胴部の長さの前記胴部の径に対する割合は、5以上10以下に設定されている、中間媒体式ガス気化器。
The intermediate-medium gas vaporizer according to any one of claims 1 to 3,
The ratio of the length of the trunk portion to the diameter of the trunk portion is an intermediate medium gas vaporizer set to 5 or more and 10 or less.
請求項1ないし4のいずれかに記載の中間媒体式ガス気化器において、
前記胴部の径の前記収容部の径に対する割合は、0.5以下に設定されている、中間媒体式ガス気化器。
The intermediate-medium gas vaporizer according to any one of claims 1 to 4,
The ratio of the diameter of the trunk portion to the diameter of the housing portion is an intermediate medium gas vaporizer set to 0.5 or less.
請求項1ないし5のいずれかに記載の中間媒体式ガス気化器において、
前記収容部の長さの前記胴部の長さに対する割合は、1.3以下に設定されている、中間媒体式ガス気化器。
The intermediate medium gas vaporizer according to any one of claims 1 to 5,
The ratio of the length of the accommodating portion to the length of the trunk portion is an intermediate medium gas vaporizer set to 1.3 or less.
請求項1ないし6のいずれかに記載の中間媒体式ガス気化器において、
前記胴部の一方側の端部に接続され、前記ガス加熱部内と連通する入口室と、
前記胴部の一方側の端部に接続され、前記ガス加熱部内と連通する出口室と、
前記胴部の一方側の端部に接続され、前記入口室と前記出口室とを仕切る仕切壁と、
前記胴部の他方側の端部に接続され、前記ガス加熱部内と連通する折り返し室と、をさらに備える、中間媒体式ガス気化器。
The intermediate medium gas vaporizer according to any one of claims 1 to 6,
An inlet chamber connected to one end of the barrel and communicating with the gas heating unit;
An outlet chamber connected to one end of the barrel and communicating with the gas heating unit;
A partition wall connected to an end portion on one side of the body portion and partitioning the inlet chamber and the outlet chamber;
An intermediate-medium gas vaporizer, further comprising: a folding chamber connected to the other end of the body and communicating with the gas heating unit.
低温液化ガスを当該低温液化ガスの沸点よりも高い沸点を有する中間媒体を用いて気化させる中間媒体式ガス気化器であって、
前記中間媒体を収容する収容部と、
前記収容部内に配置されており、熱源媒体が導入される中間媒体蒸発部と、
前記収容部内に配置されており、前記低温液化ガスが導入される低温液化ガス気化部と、
前記低温液化ガス気化部での前記低温液化ガスの気化により生じたガスが導入される筐体と、
前記筐体内に配置されており、前記熱源媒体が導入されるガス加熱部と、
前記中間媒体蒸発部へ前記熱源媒体を供給する第1熱源媒体供給流路と、
前記ガス加熱部へ前記熱源媒体を供給する第2熱源媒体供給流路と、
前記低温液化ガス気化部から流出したガスを前記筐体に導くガス流路と、を備え、
前記中間媒体蒸発部は、当該中間媒体蒸発部内を流れる前記熱源媒体と当該中間媒体蒸発部外に存在する前記中間媒体とを熱交換させることによって前記中間媒体の少なくとも一部を蒸発させ、
前記低温液化ガス気化部は、当該低温液化ガス気化部内を流れる前記低温液化ガスと当該低温液化ガス気化部外に存在する前記中間媒体とを熱交換させることによって前記低温液化ガスの少なくとも一部を気化させ、
前記ガス加熱部は、当該ガス加熱部内を流れる前記熱源媒体と当該ガス加熱部外に存在する前記ガスとを熱交換させることによって前記ガスを加熱し、
前記筐体は、
前記ガス加熱部を収容する胴部と、
前記胴部の一方側の端部に設けられており、前記ガスを前記胴部から流出させる第1流出部と、
前記胴部の他方側の端部に設けられており、前記ガスを前記胴部から流出させる第2流出部と、
前記胴部のうち前記一方側の端部と前記他方側の端部との間の部位に設けられており、前記ガスを前記胴部内に流入させる流入部と、を有し、
前記ガス流路の下流側の端部は、前記流入部に接続されている、中間媒体式ガス気化器。
An intermediate-medium gas vaporizer that vaporizes a low-temperature liquefied gas using an intermediate medium having a boiling point higher than that of the low-temperature liquefied gas,
An accommodating portion for accommodating the intermediate medium;
An intermediate medium evaporation section that is disposed in the housing section and into which the heat source medium is introduced;
A low-temperature liquefied gas vaporization section, which is disposed in the housing section and into which the low-temperature liquefied gas is introduced;
A casing into which gas generated by vaporization of the low-temperature liquefied gas in the low-temperature liquefied gas vaporization unit is introduced;
A gas heating unit disposed in the housing and into which the heat source medium is introduced;
A first heat source medium supply flow path for supplying the heat source medium to the intermediate medium evaporation section;
A second heat source medium supply channel for supplying the heat source medium to the gas heating unit;
A gas flow path for guiding the gas flowing out from the low-temperature liquefied gas vaporization section to the housing,
The intermediate medium evaporation section evaporates at least a part of the intermediate medium by exchanging heat between the heat source medium flowing in the intermediate medium evaporation section and the intermediate medium existing outside the intermediate medium evaporation section,
The low-temperature liquefied gas vaporization unit exchanges heat between the low-temperature liquefied gas flowing in the low-temperature liquefied gas vaporization unit and the intermediate medium existing outside the low-temperature liquefied gas vaporization unit, thereby at least part of the low-temperature liquefied gas Vaporize,
The gas heating unit heats the gas by exchanging heat between the heat source medium flowing in the gas heating unit and the gas existing outside the gas heating unit,
The housing is
A body portion for accommodating the gas heating unit;
A first outflow part that is provided at one end of the body part, and causes the gas to flow out of the body part;
A second outflow portion that is provided at an end portion on the other side of the body portion, and causes the gas to flow out of the body portion;
An inflow portion that is provided at a portion between the one end portion and the other end portion of the body portion, and that allows the gas to flow into the body portion;
The intermediate-medium gas vaporizer, wherein the downstream end of the gas flow path is connected to the inflow portion.
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