JPS6326178Y2 - - Google Patents

Info

Publication number
JPS6326178Y2
JPS6326178Y2 JP16010184U JP16010184U JPS6326178Y2 JP S6326178 Y2 JPS6326178 Y2 JP S6326178Y2 JP 16010184 U JP16010184 U JP 16010184U JP 16010184 U JP16010184 U JP 16010184U JP S6326178 Y2 JPS6326178 Y2 JP S6326178Y2
Authority
JP
Japan
Prior art keywords
nozzle
liquefied gas
mixing
chamber
tank
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
JP16010184U
Other languages
Japanese (ja)
Other versions
JPS6175826U (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 JP16010184U priority Critical patent/JPS6326178Y2/ja
Publication of JPS6175826U publication Critical patent/JPS6175826U/ja
Application granted granted Critical
Publication of JPS6326178Y2 publication Critical patent/JPS6326178Y2/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混合ノズル
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混合ノズルを
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 上記問題を解決するため、本考案の混合ノズル
は、中央部が筒状(断面円形または角形)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
テーパ状の噴出口を有するノズル本体を設け、該
ノズル本体内の中央部の中間位置から噴出口まで
にこのノズル本体内の下流側を2室に分ける仕切
板を設け、一方の室内に減速用充填物を充填した
ものである。
Means for Solving the Problems In order to solve the above problems, the mixing nozzle of the present invention has a central part formed in a cylindrical shape (circular or square cross section), a receiving port at the base end, and a distal end. A nozzle body is provided with a tapered jet nozzle, and a partition plate is provided from an intermediate position in the center of the nozzle body to the jet nozzle to divide the downstream side of the nozzle body into two chambers, and one of the chambers has a deceleration chamber. It is filled with a filler for use.

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仕
切板で2流に分かれ、一方流は一方室の充填物に
当たつて減速させられ、噴出口から比較的ゆつく
り噴出させられる。また他方流は他方室を通つて
噴出口から勢いよく噴出させられる。そして噴出
口の前方では、ゆつくり噴出させられる一方流と
勢いよく噴出させられる他方流とが互いに干渉し
あい、これによつて渦が発生し、液化ガスが混合
撹拌させられるものである。
Effect In the above configuration, when the mixing nozzle is installed in the liquefied gas circulation path of a large liquefied gas storage tank, for example, the liquefied gas that enters the central part from the intake port is divided into two streams by the partition plate, and one stream flows into one chamber. When it hits the filling material, it is decelerated and is ejected from the ejection port relatively slowly. The other flow passes through the other chamber and is forcefully jetted out from the spout. In front of the spout, one stream that is slowly ejected and the other stream that is ejected vigorously interfere with each other, thereby generating a vortex and mixing and stirring the liquefied gas.

実施例 以下、本考案の一実施例を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混合ノズルであつて、中央部
6Aが円筒状(角筒状でもよい)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テー
パ状の噴出口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の中間位置から噴出口
6Cまでに配設されて、ノズル本体6内の下流側
を2室7,8に分ける仕切板9と、一方室7内の
上流側に充填された多数の減速用ビース状充填物
10と、中央部6Aの下流側に両室7,8にわた
つて配設されたハニカム格子からなる整流板11
と、一方室7の上流端に配設された充填物支持用
網12とから構成されている。
Embodiment Hereinafter, an embodiment of the present invention will be described based on the drawings. Reference numeral 1 denotes a large tank for storing liquefied gas 2 such as LPG or LNG, and 3 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 central portion 6A formed in a cylindrical shape (or a rectangular tube shape) and a receiving port 6B at the base end. The nozzle main body 6 has a tapered jet nozzle 6C at the tip, and the nozzle main body 6 is arranged from an intermediate position between the central part 6A and the nozzle nozzle 6C, and the downstream side of the nozzle main body 6 is divided into two chambers. A partition plate 9 dividing the chamber 7 and 8, a large number of deceleration beads 10 filled upstream of one chamber 7, and a plurality of deceleration beads 10 disposed downstream of the central portion 6A across both chambers 7 and 8. A rectifying plate 11 made of a honeycomb lattice
and a filling support net 12 disposed at the upstream end of one chamber 7.

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、
混合ノズル5内に吐出させられる。すると、その
混合ノズル5内に入つた液化ガス2は仕切板9で
2流A,Bに分かれ、一方流Aは一方室7の充填
物10に当たつて減速させられ、整流板11で流
れを整えられた後、噴出口6Cから比較的ゆつく
り噴出させられる。また他方流Bは他方室8を通
つて整流板11に流れを整えられた後、噴出口6
Cから勢いよく噴出させられる。そして噴出口6
Cの前方では、ゆつくり噴出させられる一方流A
と勢いよく噴出させられる他方流Bとが互いに干
渉しあい、これによつて強い二次元渦Cが発生
し、液化ガス2が混合撹拌させられるものであ
る。なお第2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 entered the mixing nozzle 5 is divided into two streams A and B by the partition plate 9, one stream A hits the filling 10 in the other chamber 7 and is decelerated, and the flow is changed by the rectifier plate 11. After this, the water is ejected relatively slowly from the ejection port 6C. The other flow B passes through the other chamber 8 and is adjusted by the current plate 11, and then flows through the jet nozzle 6.
It is made to gush forcefully from C. and spout 6
In front of C, one-sided flow A is slowly ejected.
and the other flow B which is ejected vigorously interfere with each other, thereby generating a strong two-dimensional vortex C, which mixes and stirs the liquefied gas 2. Note that in FIG. 2, A is a velocity distribution diagram.

上記混合ノズル5は、液化ガス2の混合の他、
種々の液体の混合に用いることができるものであ
つて、大型タンク設備先、大きな密度差を有する
混合物の貯蔵を必要とするユーザの要望にこたえ
ることができるものである。
In addition to mixing the liquefied gas 2, the mixing nozzle 5 also mixes the liquefied gas 2.
It can be used to mix various liquids, and can meet the needs of users who require large tank installations and storage of mixtures with large density differences.

考案の効果 以上述べたごとく本考案によれば、噴出口から
流速の異なる2つの流れが同時に噴出させられ、
その2つの流れが互いに干渉しあつて渦が発生
し、液体が混合撹拌させられるものである。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, two flows with different flow velocities are ejected from the spout at the same time,
When these two flows interfere with each other, a vortex is generated, and the liquid is mixed and agitated. Therefore, in large storage tanks for LPG, LNG, etc.
It is ideal for destroying the stratification phenomenon of liquids, has a simple and inexpensive structure, and uses the flow of liquid, so no special driving source is required.

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

図は本考案の一実施例を示し、第1図はタンク
の概略縦断面図、第2図は要部の縦断面図、第3
図は第2図の−矢視図である。 5……混合ノズル、6……ノズル本体、6A…
…中央部、6B……受入口、6C……噴出口、
7,8……室、9……仕切板、10……充填物。
The figures show one embodiment of the present invention, in which Figure 1 is a schematic vertical cross-sectional view of the tank, Figure 2 is a vertical cross-sectional view of the main part, and Figure 3 is a vertical cross-sectional view of the main part.
The figure is a view taken along the - arrow in FIG. 5...Mixing nozzle, 6...Nozzle body, 6A...
...Central part, 6B...Intake port, 6C...Spout port,
7, 8...chamber, 9...partition plate, 10...filler.

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テーパ状の噴出口を有する
ノズル本体を設け、該ノズル本体内の中央部の中
間位置から噴出口までにこのノズル本体内の下流
側を2室に分ける仕切板を設け、一方の室内に減
速用充填物を充填したことを特徴とする混合ノズ
ル。
A nozzle body is provided in which the central part is formed into a cylindrical shape and has a receiving port at the base end and a tapered jet port at the distal end. A mixing nozzle characterized in that a partition plate is provided to divide the downstream side of the nozzle body into two chambers, and one chamber is filled with a deceleration filler.
JP16010184U 1984-10-22 1984-10-22 Expired JPS6326178Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16010184U JPS6326178Y2 (en) 1984-10-22 1984-10-22

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16010184U JPS6326178Y2 (en) 1984-10-22 1984-10-22

Publications (2)

Publication Number Publication Date
JPS6175826U JPS6175826U (en) 1986-05-22
JPS6326178Y2 true JPS6326178Y2 (en) 1988-07-15

Family

ID=30718031

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16010184U Expired JPS6326178Y2 (en) 1984-10-22 1984-10-22

Country Status (1)

Country Link
JP (1) JPS6326178Y2 (en)

Also Published As

Publication number Publication date
JPS6175826U (en) 1986-05-22

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