JPS6346102Y2 - - Google Patents

Info

Publication number
JPS6346102Y2
JPS6346102Y2 JP1984166548U JP16654884U JPS6346102Y2 JP S6346102 Y2 JPS6346102 Y2 JP S6346102Y2 JP 1984166548 U JP1984166548 U JP 1984166548U JP 16654884 U JP16654884 U JP 16654884U JP S6346102 Y2 JPS6346102 Y2 JP S6346102Y2
Authority
JP
Japan
Prior art keywords
liquefied gas
nozzle
tank
spiral
mixing
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.)
Expired
Application number
JP1984166548U
Other languages
Japanese (ja)
Other versions
JPS6183436U (en
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 filed Critical
Priority to JP1984166548U priority Critical patent/JPS6346102Y2/ja
Publication of JPS6183436U publication Critical patent/JPS6183436U/ja
Application granted granted Critical
Publication of JPS6346102Y2 publication Critical patent/JPS6346102Y2/ja
Expired legal-status Critical Current

Links

Description

【考案の詳細な説明】 産業上の利用分野 本考案はLPG、LNG等の貯蔵大型タンク等に
おける貯蔵液体を混合撹拌するためのミキシング
ノズルに関するものである。
[Detailed Description of the Invention] Industrial Application Field The present invention relates to a mixing nozzle for mixing and agitating liquids stored in large tanks for storing LPG, LNG, etc.

従来の技術 たとえばLPG、LNG等の液化ガスの貯蔵大型
タンクでは、わずかな温度差の相違によつて液化
ガスの密度(組成)が異なり、層状化現象が発生
する。そこで従来では、液化ガスを循環させてい
る。
Conventional Technology For example, in large storage tanks for liquefied gases such as LPG and LNG, the density (composition) of the liquefied gas varies due to slight differences in temperature, causing a stratification phenomenon. Therefore, conventionally, liquefied gas is circulated.

考案が解決しようとする問題点 上記従来構成によれば、液化ガスを循環させて
いるだけであるので、層状化現象を完全に解消す
ることができない。そこでタンクに混合撹拌装置
を設けることが考えられるが、これではその混合
撹拌装置が比較的高価であることと、その装置を
作動させるための特別の動力が必要であることか
ら、コストアツプになるものである。
Problems to be Solved by the Invention According to the above-mentioned conventional configuration, since the liquefied gas is simply circulated, the stratification phenomenon cannot be completely eliminated. Therefore, it is possible to install a mixing and stirring device in the tank, but this would increase costs because the mixing and stirring device is relatively expensive and special power is required to operate the device. It is.

本考案はかかる問題点を解消したミキシングノ
ズルを提供するものである。
The present invention provides a mixing nozzle that solves these problems.

問題点を解決するための手段 上記目的を達成するため、本考案のミキシング
ノズルは、中央部が筒状に形成されると共に基端
部に受入口を有しかつ先端部に小径の噴出口を有
するノズル本体を設け、該ノズル本体中央部に多
数の螺旋穴を有する断面がハニカム状の構造体を
内蔵したものである。
Means for Solving the Problems In order to achieve the above object, the mixing nozzle of the present invention has a cylindrical central portion, a receiving port at the base end, and a small diameter jet port at the distal end. A nozzle body is provided, and a structure having a honeycomb-like cross section and having a large number of spiral holes is built in the center of the nozzle body.

作 用 上記構成において、混合ノズルを、たとえば液
化ガス貯蔵大型タンクの液化ガス循環経路に配設
すると、受入口から中央部に入つた液化ガスは多
数の螺旋穴を有する断面がハニカム状の構造体に
よつて螺旋流にされ、その螺旋流は噴出口で流速
を早められた後、タンク内に噴射され、液化ガス
を混合撹拌する。
Effect In the above configuration, when the mixing nozzle is arranged, for example, in the liquefied gas circulation path of a large liquefied gas storage tank, the liquefied gas that enters the central part from the receiving port is sent to a structure with a honeycomb-like cross section that has many spiral holes. The spiral flow is made into a spiral flow by the jet, and after the flow speed is increased at the jet port, the spiral flow is injected into the tank to mix and stir the liquefied gas.

実施例 以下、本考案の一実施例を第1図〜第3図に基
づいて説明する。1はLPG、LNG等の液化ガス
2の貯蔵大型タンク、3は該タンク1の上部と下
部とをつなぐ循環パイプであつて、途中にポンプ
4を介在させてある。5はタンク1内において循
環パイプ3の吐出口に接続されたミキシングノズ
ルであつて、中央部6Aが円筒状に形成されると
共に基端部に受入口6Bを有しかつ先端部に小径
の噴出口6cを有するノズル本体6と、該ノズル
本体6内の中央部6Aの後流側に多数の螺旋穴7
を有する断面がハニカム状の構造体8とから構成
されている。
Embodiment An embodiment of the present invention will be described below with reference to FIGS. 1 to 3. 1 is a large tank for storing liquefied gas 2 such as LPG or LNG, and 3 is a circulation pipe connecting the upper and lower parts of the tank 1, with a pump 4 interposed in the middle. Reference numeral 5 denotes a mixing nozzle connected to the discharge port of the circulation pipe 3 in the tank 1, which has a cylindrical central portion 6A, a receiving port 6B at the base end, and a small diameter jet at the tip. A nozzle body 6 having an outlet 6c, and a large number of spiral holes 7 on the downstream side of the central part 6A in the nozzle body 6.
The structural body 8 has a honeycomb-like cross section.

以下、上記構成における作用について説明す
る。まずポンプ4を作動させると、タンク1内の
液化ガス2の上部がパイプ3を介して吸引され、
ミキシングノズル5内に吐出させられる。する
と、そのミキシングノズル5内に入つた液化ガス
2はハニカム構造体8の螺旋穴7を通過し、これ
によつて螺旋状の整流が形成される。その螺旋状
の整流に形成された液化ガス2は噴出口6cを通
過する際に流速を早められ、勢いよくタンク1内
に噴出させられる。そして噴出口6cの前方にお
いてミキシングノズル5の軸心方向に沿つて強い
渦流が比較的長い距離にわたつて形成され、タン
ク1内の液化ガス2を混合撹拌するものである。
なお、第1図においてイは速度分布図である。
Hereinafter, the effects of the above configuration will be explained. First, when the pump 4 is activated, the upper part of the liquefied gas 2 in the tank 1 is sucked through the pipe 3.
It is discharged into the mixing nozzle 5. Then, the liquefied gas 2 that has entered the mixing nozzle 5 passes through the spiral hole 7 of the honeycomb structure 8, thereby forming a spiral rectification. The liquefied gas 2 formed in the spirally rectified flow has a faster flow rate when passing through the ejection port 6c, and is forcefully ejected into the tank 1. A strong vortex is formed over a relatively long distance in front of the ejection port 6c along the axial direction of the mixing nozzle 5, and mixes and stirs the liquefied gas 2 in the tank 1.
Note that in FIG. 1, A is a velocity distribution diagram.

考案の効果 以上述べたごとく本考案によれば、多数の螺旋
穴を有する断面ハニカム状の構造体によつて螺旋
流を形成し、その螺旋流によつて液体を混合撹拌
することができるものである。したがつてLPG、
LNG等の貯蔵大型タンクにおいて、液体の層状
化現象を破壊するのに最適であり、また構造が簡
単で安価であり、液体の流れを利用するものであ
るから、特別の駆動源が不用である。
Effects of the invention As described above, according to the invention, a spiral flow is formed by a honeycomb-like cross-sectional structure having a large number of spiral holes, and liquid can be mixed and stirred by the spiral flow. be. Therefore LPG,
It is ideal for destroying the stratification phenomenon of liquids in large storage tanks such as LNG, and the structure is simple and inexpensive, and since it utilizes the flow of liquid, no special driving source is required. .

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

第1図〜第3図は本考案の一実施例を示し、第
1図は縦断面図、第2図は第1図の−矢視
図、第3図は貯蔵大型タンクの縦断面図である。 2……液化ガス、5……ミキシングノズル、6
……ノズル本体、6A……中央部、6B……受入
口、6c……噴出口、7……螺旋穴、8……ハニ
カム構造体。
Figures 1 to 3 show one embodiment of the present invention, with Figure 1 being a longitudinal sectional view, Figure 2 being a view taken along the - arrow in Figure 1, and Figure 3 being a longitudinal sectional view of a large storage tank. be. 2...Liquified gas, 5...Mixing nozzle, 6
... Nozzle body, 6A ... Central part, 6B ... Intake port, 6c ... Spout port, 7 ... Spiral hole, 8 ... Honeycomb structure.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 中央部が筒状に形成されると共に基端部に受入
口を有しかつ先端部に小径の噴出口を有するノズ
ル本体を設け、該ノズル本体中央部に多数の螺旋
穴を有する断面がハニカム状の構造体を内蔵した
ことを特徴とするミキシングノズル。
A nozzle body is provided, the central part of which is formed into a cylindrical shape, and which has a receiving port at the base end and a small-diameter jet nozzle at the distal end, and has a honeycomb-shaped cross section with a large number of spiral holes in the central part of the nozzle body. A mixing nozzle characterized by having a built-in structure.
JP1984166548U 1984-11-02 1984-11-02 Expired JPS6346102Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1984166548U JPS6346102Y2 (en) 1984-11-02 1984-11-02

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1984166548U JPS6346102Y2 (en) 1984-11-02 1984-11-02

Publications (2)

Publication Number Publication Date
JPS6183436U JPS6183436U (en) 1986-06-02
JPS6346102Y2 true JPS6346102Y2 (en) 1988-12-01

Family

ID=30724356

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1984166548U Expired JPS6346102Y2 (en) 1984-11-02 1984-11-02

Country Status (1)

Country Link
JP (1) JPS6346102Y2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5352689Y2 (en) * 1973-10-11 1978-12-16

Also Published As

Publication number Publication date
JPS6183436U (en) 1986-06-02

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