JPH04169790A - Open rack type vaporizer - Google Patents

Open rack type vaporizer

Info

Publication number
JPH04169790A
JPH04169790A JP2296970A JP29697090A JPH04169790A JP H04169790 A JPH04169790 A JP H04169790A JP 2296970 A JP2296970 A JP 2296970A JP 29697090 A JP29697090 A JP 29697090A JP H04169790 A JPH04169790 A JP H04169790A
Authority
JP
Japan
Prior art keywords
header tank
tank
liquefied gas
water
rack type
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2296970A
Other languages
Japanese (ja)
Other versions
JP2631033B2 (en
Inventor
Mamoru Okada
衛 岡田
Kanji Kujirai
鯨井 寛司
Katsumasa Ishikawa
石川 勝政
Sadao Sugawara
菅原 貞雄
Hideo Koike
小池 秀男
Yoji Sato
洋治 佐藤
Masaru Akiyama
優 秋山
Yoshitoshi Nakamura
中村 義俊
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sumitomo Precision Products Co Ltd
Tokyo Gas Co Ltd
Original Assignee
Sumitomo Precision Products Co Ltd
Tokyo Gas Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sumitomo Precision Products Co Ltd, Tokyo Gas Co Ltd filed Critical Sumitomo Precision Products Co Ltd
Priority to JP2296970A priority Critical patent/JP2631033B2/en
Publication of JPH04169790A publication Critical patent/JPH04169790A/en
Application granted granted Critical
Publication of JP2631033B2 publication Critical patent/JP2631033B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D3/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium flows in a continuous film, or trickles freely, over the conduits
    • F28D3/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium flows in a continuous film, or trickles freely, over the conduits with tubular conduits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D3/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium flows in a continuous film, or trickles freely, over the conduits
    • F28D3/04Distributing arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0061Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for phase-change applications
    • F28D2021/0064Vaporizers, e.g. evaporators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2270/00Thermal insulation; Thermal decoupling

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PURPOSE:To prevent bowing generated at a lower header tank by introducing liquefied gas from an upper header tank, sprinkling water from sprinklers arranged above a standing panel to vaporize the gas, and feeding down the evaporated gas from the lower tank. CONSTITUTION:The upper ends of fin tubes connected to the entire outer periphery of an upper header tank 2 are covered with a heat insulator 6 to be insulated. Overflowing water from a sprinkler 4 is first brought into contact with the insulator 6 under the tank 2, and then fed down on a heat exchanging panel 1. With such a structure, liquefied gas is introduced from the tank 2, heat exchanged with parallel flow of sprinkled marine water to be vaporized, and discharged from a lower header tank 3 to constitute a down-flow type vaporizer. Since the tank 2 and the vicinity are insulated, a temperature difference between the upper and lower surfaces of a tube does not occur, and hence bowing can be eliminated.

Description

【発明の詳細な説明】 利用産業分野 この発明は、液化天然ガスを気化するためのオープンラ
ック型気化器に係り、フィンチューブを連立した熱交換
パネルの上部ヘッダータンクより液化ガスを導入し、散
水した熱媒体と並流熱交換させるダウンフロー成型気化
器となし、従来アップフロー式気化器のヘッダータンク
に発生するボーイング現象、カロリーハンチング現象を
防止したダウンフロー式のオープンラック型気化器に関
する。
[Detailed Description of the Invention] Field of Application This invention relates to an open rack type vaporizer for vaporizing liquefied natural gas, in which liquefied gas is introduced from an upper header tank of a heat exchange panel with a series of fin tubes, and water is sprinkled. This invention relates to a down-flow molded vaporizer that exchanges heat in parallel with a heated heat medium, and a down-flow open rack vaporizer that prevents the bowing phenomenon and calorie hunting phenomenon that occur in the header tank of conventional up-flow vaporizers.

背景技術 オープンラック型気化器は、例えば、第3図、第4図に
示す如く、直径方向に一対のフィンを突出させたフィン
チューブをフィン方向に配列して一枚のパネル状となし
、その上下端部ばヘッダータンク(2X3)を設けて熱
交換パネル(1)を構成し、該パネルを複数連立配置し
て、熱交換パネル(1)の上方に配設した散水器(4)
より熱媒体の海水を熱交換パネル(1)面に流下させる
構造である。
BACKGROUND ART As shown in FIGS. 3 and 4, for example, an open rack type vaporizer has a fin tube in which a pair of fins protrudes in the diametrical direction and is arranged in the fin direction to form a single panel. A heat exchange panel (1) is constructed by providing header tanks (2×3) at the upper and lower ends, and a water sprinkler (4) is arranged above the heat exchange panel (1) by arranging a plurality of such panels in parallel.
This structure allows seawater, which is a heat medium, to flow down onto the surface of the heat exchange panel (1).

上記従来気化器の熱交換機構は、第3図に示す如く、超
低温の液化ガスを下部ヘッダータンク(3)から各フィ
ンチューブに流入させて気化させ、常温のガスとして上
部ヘッダータンク(2)へ送出するフローであり、所謂
アップフローと呼ばれるものである。
As shown in Fig. 3, the heat exchange mechanism of the conventional vaporizer described above is such that ultra-low temperature liquefied gas flows from the lower header tank (3) into each fin tube and is vaporized, and is then transferred to the upper header tank (2) as room temperature gas. This is a flow to be sent out, and is what is called an upflow.

オープンラック型気化器のアップフローにおいて、下部
ヘッダータンク(3)は、その管下部側は超低温の液体
であるのに対して、管上部側は熱源の散水による入熱を
受けるために下部に比べ高温となり、そのため管上、下
部に温度差が生じ、第3図に想偉線に示す如く弓なりの
ボーイング現象を生じる。
In the upflow of an open rack type vaporizer, the lower header tank (3) has ultra-low temperature liquid in the lower part of the pipe, while the upper part of the pipe receives heat input from the water sprinkling from the heat source, so it has a lower temperature than the lower part. The temperature becomes high, which causes a temperature difference between the top and bottom of the tube, causing a bowing phenomenon as shown by the Wei line in Figure 3.

かかるボーイング現象が発生すると、フィンチューブの
下部、特に、組立時のヘッダータンクとの溶接のために
組立時フィン下端部を切除した部分が曲り、かつフィン
切除に伴なう形状変化による応力の増大によって内部及
び装置が損傷する恐れがあるなど耐久性に問題があり、
これを防止するため、フィン切除部に溶接肉盛する(実
公平l。
When such a bowing phenomenon occurs, the lower part of the fin tube, especially the part where the lower end of the fin is cut off during assembly to be welded to the header tank during assembly, becomes bent, and stress increases due to the change in shape caused by the fin cutting. There are durability issues such as the possibility of damage to the internal parts and equipment due to
In order to prevent this, weld overlay on the fin cut-out part (Actually, it is not fair).

20549号公報)などの対策が必要となる。20549 Publication) etc. are required.

また、アップフローでは、上記同様下部ヘッダータンク
(3)に入熱を受けることにより、特に、負荷の小さい
低流量時にヘッダー内部の液体が蒸発を起こし、このた
め送出ガス流量及びカロリーにハンチング現象を生じる
問題がある。
In addition, in upflow, the heat input to the lower header tank (3) as described above causes the liquid inside the header to evaporate, especially at low flow rates with small loads, which causes a hunting phenomenon in the delivered gas flow rate and calories. There are problems that arise.

発明の概要 この発明は、上述の現状に鑑み、下部ヘッダータンクに
発生するボーイング現象を防止してパネルの寿命を延長
でき、かつ構造が簡単で付設が容易な構成のオープンラ
ック型気化器を目的に種々検討した結果、ヘッダータン
ク内部の低温液体が散水による影響を受けないよう、超
低温の液体は上部ヘッダータンクに導入し、常温のガス
を下部ヘッダータンクに送出するダウンフロー式気化器
とすることにより、構成が簡単で熱交換効率にすぐれ、
ハンチング現象がなくなり、耐久性にすぐれたオープン
ラック型気化器が得られることを知見したものである。
Summary of the Invention In view of the above-mentioned current situation, the object of the present invention is to provide an open rack type carburetor that can prevent the bowing phenomenon that occurs in the lower header tank and extend the life of the panel, and that has a simple structure and is easy to install. As a result of various studies, in order to prevent the low-temperature liquid inside the header tank from being affected by water spraying, we decided to use a down-flow type vaporizer that introduces the ultra-low temperature liquid into the upper header tank and sends room temperature gas to the lower header tank. The structure is simple and the heat exchange efficiency is excellent.
It was discovered that an open rack type vaporizer that eliminates the hunting phenomenon and has excellent durability can be obtained.

すなわち、この発明は、 フィンチューブを連立し上下端にヘッダータンクを設け
て熱交換パネルを構成し、 上部ヘッダータンクより液化ガスを導入し、立設する該
パネル上方に各々配設した散水器より散水して液化ガス
を気化させ、下部ヘッダータンクより気化ガスを導出す
るダウンフローであることを特徴とするオープンラック
型気化器である。
That is, the present invention comprises a heat exchange panel with fin tubes arranged in series and header tanks provided at the upper and lower ends, liquefied gas is introduced from the upper header tank, and water sprinklers are installed above each of the upright panels. This is an open rack type vaporizer that is characterized by a downflow system that vaporizes liquefied gas by sprinkling water and extracts the vaporized gas from a lower header tank.

また、この発明は、上記構成において、a、上部ヘッダ
ータンク内に複数の上向き噴出孔を有するスパージパイ
プを挿入して均等に分流するよう液化ガスを導入し、 b、上部ヘッダータンク全体及びその直近のフィンチュ
ーブ外面に断熱材を付設して保冷して他の入熱を遮断し
、断熱材を付設したフィンチューブ部分より散水可能と
なして氷結防止し、C1各フィンチューブ内にスパイラ
ルプレートやスパイラルコアなどの乱流促進材を挿入し
て液の自由落下を防止したことを特徴とするオープンラ
ック型気化器である。
In addition, in the above configuration, the present invention includes: a) inserting a sparge pipe having a plurality of upward spout holes into the upper header tank and introducing the liquefied gas so as to divide the flow evenly; and b) the entire upper header tank and its immediate vicinity. A heat insulating material is attached to the outer surface of the fin tube to keep it cool and block other heat input.Water can be sprinkled from the fin tube part with the insulating material attached to prevent freezing, and a spiral plate or spiral core is installed inside each C1 fin tube. This is an open rack type vaporizer characterized by inserting a turbulence promoting material such as turbulence promoting material to prevent free fall of the liquid.

発明の図面に基づく開示 第1図はこの発明によるオープンラック型気化器の正面
説明図である。第2図はその上部ヘッダータンク及び散
水器を示す縦断側面説明図である。
DISCLOSURE OF THE INVENTION BASED ON DRAWINGS FIG. 1 is an explanatory front view of an open rack type vaporizer according to the present invention. FIG. 2 is a longitudinal side view showing the upper header tank and water sprinkler.

構成 第1図に示す如く、この発明によるオープンラック型気
化器は、例えば、周囲に複数対のフィンを突出させたフ
ィンチューブを所定のフィン方向に配列して一枚のパネ
ル状となし、その上端及び下端部にヘッダータンク(2
X3)を設けて熱交換パネル(1)を構成し、図示しな
いが、この熱交換パネル(1)を複数亜列吊支し、各ヘ
ッダータンクはそれぞれ1本のマニホールドに直交接続
される。
Structure As shown in FIG. 1, the open rack type carburetor according to the present invention has, for example, a fin tube with a plurality of pairs of fins protruding from the periphery arranged in a predetermined fin direction to form a single panel. Header tanks (2
Although not shown, the heat exchange panels (1) are suspended in a plurality of sub-rows, and each header tank is orthogonally connected to one manifold.

すなわち、上部ヘッダータンク(2)は液化ガス供給用
のマニホールドに直交接続され、下部ヘッダータンク(
3)は気化ガス導出用のマニホールドに直交接続される
That is, the upper header tank (2) is orthogonally connected to the liquefied gas supply manifold, and the lower header tank (2) is orthogonally connected to the liquefied gas supply manifold.
3) is orthogonally connected to a manifold for deriving vaporized gas.

また、上部ヘッダータンク(2)は、複数の噴出孔を上
向きに明けたスパージパイプ(5)を挿入してあり、供
給される液化ガスを熱交換パネル(1)の各フィンチュ
ーブに均等に分流させることができる。
In addition, the upper header tank (2) has a sparge pipe (5) inserted therein which has multiple ejection holes facing upward, and distributes the supplied liquefied gas evenly to each fin tube of the heat exchange panel (1). be able to.

図示しないが、熱交換パネル(1)の各フィンチューブ
内には、液化ガスの自白落下を防止し、熱交換効率を向
上させる乱流促進材を挿入しである。乱流促進材には、
−枚板を捻じったスパイラルプレートや断面十字型の形
材棒を捻じったスパイラルコアなどを用いることができ
る。
Although not shown, a turbulence promoting material is inserted into each fin tube of the heat exchange panel (1) to prevent the liquefied gas from falling and improve the heat exchange efficiency. Turbulence promoting materials include:
- A spiral plate made of twisted sheets or a spiral core made of a twisted cross-section rod can be used.

第2図に示す如く、熱交換パネル(1)の上方に配設し
た散水器(4)より熱媒体の海水を溢水させて熱交換パ
ネル(1)面を流下させる構造であるが、上部ヘッダー
タンク(2)の外周面全体と接続される各フィンチュー
ブの上端部を断熱材(6)で被覆して保冷し、散水器(
4)よりの溢水がまず上部ヘッダータンク(2)下方の
断熱材(6)に当たってがら熱交換パネル(1)面を流
下する構成である。
As shown in Fig. 2, the structure is such that seawater as a heat medium overflows from the water sprinkler (4) placed above the heat exchange panel (1) and flows down the surface of the heat exchange panel (1). The upper end of each fin tube connected to the entire outer circumferential surface of the tank (2) is covered with a heat insulating material (6) to keep it cool, and the water sprinkler (
4) The overflowing water first hits the insulation material (6) below the upper header tank (2) and then flows down the surface of the heat exchange panel (1).

作用効果 かかる構造により、この発明によるオープンラック型気
化器は、上部ヘッダータンク(2)より液化ガスを導入
し、熱交換パネル(1)の各フィンチューブを落下す゛
る間に、液化ガスは散水した海水と並流熱交換して気化
し、下部ヘッダータンク(3)より導出されるダウンフ
ロー式気化器を構成している。
Effects With this structure, the open rack type vaporizer according to the present invention introduces liquefied gas from the upper header tank (2), and while it falls through each fin tube of the heat exchange panel (1), the liquefied gas is sprinkled with water. It vaporizes by co-current heat exchange with seawater, and constitutes a down-flow vaporizer that is led out from the lower header tank (3).

上部ヘッダータンク(2)のスパージパイプ(5)の挿
入により、熱交換パネル(1)には液化ガスが均等に分
配されて安定した熱交換性能を得ることができる。
By inserting the sparge pipe (5) in the upper header tank (2), the liquefied gas is evenly distributed in the heat exchange panel (1), and stable heat exchange performance can be obtained.

また、上部ヘッダータンク(2)とその近傍を保冷をし
ているため、上部ヘッダータンク(2)に超低温の液化
ガスが流入しても、管周囲は保冷により他の入熱を受け
ることがなく、ハンチング現象がなくなり、さらに、管
上下面の温度差も生じないために、ボーイング現象もな
くすことができ、気化器全体の耐久性が著しく向上する
In addition, since the upper header tank (2) and its vicinity are kept cool, even if ultra-low temperature liquefied gas flows into the upper header tank (2), the area around the pipes will not receive any other heat input due to the cold insulation. Since the hunting phenomenon is eliminated and there is no temperature difference between the upper and lower surfaces of the tube, the bowing phenomenon can also be eliminated, and the durability of the entire vaporizer is significantly improved.

さらに、上部ヘッダータンク(2)と熱交換パネル(1
)上部に保冷施工してその保冷部に散水させるため、散
水近傍部の氷結は発生せず、良好な散水状態を得ること
ができ、安定した熱交換性能を得ることができる。
Furthermore, the upper header tank (2) and the heat exchange panel (1)
) Since cold insulation is installed on the upper part and water is sprinkled on the cold insulation part, freezing does not occur in the area near the water spraying, a good water sprinkling condition can be obtained, and stable heat exchange performance can be obtained.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はこの発明によるダウンフロー式のオープンラッ
ク型気化器の正面説明図である。第2図はその上部ヘッ
ダータンク及び散水器を示す縦断側面説明図である。 第3図、第4図は従来のアップフロー式のオープンラッ
ク型気化器の正面説明図と側面説明図である。 1・・・熱交換パネル、2・・・上部ヘッダータンク、
3・・・下部ヘッダータンク、4・・・散水器、5・・
・スパージパイプ、6・・・断熱材。
FIG. 1 is an explanatory front view of a down-flow open rack type vaporizer according to the present invention. FIG. 2 is a longitudinal side view showing the upper header tank and water sprinkler. FIGS. 3 and 4 are a front view and a side view of a conventional up-flow open rack type carburetor. 1... Heat exchange panel, 2... Upper header tank,
3... Lower header tank, 4... Water sprinkler, 5...
・Sparge pipe, 6...insulation material.

Claims (1)

【特許請求の範囲】 1 フィンチューブを連立し上下端にヘッダータンクを設け
て熱交換パネルを構成し、上部ヘッダータンクより液化
ガスを導入し、立設する該パネル上方に各々配設した散
水器より散水して液化ガスを気化させ、下部ヘッダータ
ンクより気化ガスを導出するダウンフローであることを
特徴とするオープンラック型気化器。 2 上部ヘッダータンク内に複数の上向き噴出孔を有するス
パージパイプを挿入して液化ガスを導入し、上部ヘッダ
ータンク全体及びその直近のフィンチューブ外面に断熱
材を付設して保冷し、断熱材を付設したフィンチューブ
部分より散水可能となし、各フィンチューブ内に乱流促
進材を挿入したことを特徴とする請求項1記載のオープ
ンラック型気化器。
[Scope of Claims] 1 A heat exchange panel is constructed by arranging fin tubes and providing header tanks at the upper and lower ends, and liquefied gas is introduced from the upper header tank, and water sprinklers are respectively arranged above the upright panels. This open rack type vaporizer is characterized by a down-flow system that vaporizes liquefied gas by sprinkling water and extracting the vaporized gas from a lower header tank. 2. A sparge pipe with multiple upward spouting holes was inserted into the upper header tank to introduce liquefied gas, and insulation was attached to the entire upper header tank and the outer surface of the fin tube in its immediate vicinity to keep it cool. 2. The open rack type vaporizer according to claim 1, wherein water can be sprinkled from the fin tube portion, and a turbulence promoting material is inserted into each fin tube.
JP2296970A 1990-10-31 1990-10-31 Open rack type vaporizer Expired - Lifetime JP2631033B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2296970A JP2631033B2 (en) 1990-10-31 1990-10-31 Open rack type vaporizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2296970A JP2631033B2 (en) 1990-10-31 1990-10-31 Open rack type vaporizer

Publications (2)

Publication Number Publication Date
JPH04169790A true JPH04169790A (en) 1992-06-17
JP2631033B2 JP2631033B2 (en) 1997-07-16

Family

ID=17840563

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2296970A Expired - Lifetime JP2631033B2 (en) 1990-10-31 1990-10-31 Open rack type vaporizer

Country Status (1)

Country Link
JP (1) JP2631033B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100482825B1 (en) * 2002-07-09 2005-04-14 삼성전자주식회사 Heat exchanger

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5821195A (en) * 1981-07-29 1983-02-07 株式会社日立製作所 Control rod drive mechanism for reactor

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5821195A (en) * 1981-07-29 1983-02-07 株式会社日立製作所 Control rod drive mechanism for reactor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100482825B1 (en) * 2002-07-09 2005-04-14 삼성전자주식회사 Heat exchanger

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