JPS6327830Y2 - - Google Patents
Info
- Publication number
- JPS6327830Y2 JPS6327830Y2 JP3537681U JP3537681U JPS6327830Y2 JP S6327830 Y2 JPS6327830 Y2 JP S6327830Y2 JP 3537681 U JP3537681 U JP 3537681U JP 3537681 U JP3537681 U JP 3537681U JP S6327830 Y2 JPS6327830 Y2 JP S6327830Y2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- skim
- liquid
- collector
- roof plate
- 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
Links
- 239000007788 liquid Substances 0.000 claims description 33
- 238000000926 separation method Methods 0.000 claims description 14
- 230000003028 elevating effect Effects 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 19
- 230000005484 gravity Effects 0.000 description 7
- 238000007634 remodeling Methods 0.000 description 3
- 238000005452 bending Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000003014 reinforcing effect Effects 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- 230000003139 buffering effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Removal Of Floating Material (AREA)
Description
【考案の詳細な説明】
この考案は、例えば水分と油分等比重の異る液
成分が混合した原液が分離タンク内で層化させら
れた後の上層の軽質成分をスキミングし固有の排
出ノズルから取出し得るようにした液分離装置に
関するものである。[Detailed explanation of the invention] This invention is based on a method in which, after a raw solution containing liquid components of different specific gravities, such as water and oil, is stratified in a separation tank, the light components in the upper layer are skimmed through a unique discharge nozzle. This invention relates to a liquid separation device that can be taken out.
例えばタンカから排出された大量のバラスト水
には、船内の廃油が多少混入していることから、
原水のまゝで外部投棄することが許されず、この
ことから、処理されるバラスト水は、一旦分離タ
ンクに貯蔵されることにより、比重差に基づいて
水分と油分ごとに層化分離され、その後、油分は
固別の排出ノズルから取出しかつ処分されるのが
普通である。 For example, a large amount of ballast water discharged from a tanker contains some amount of waste oil from the ship.
It is not allowed to dump raw water outside, so the ballast water to be treated is once stored in a separation tank where it is stratified and separated into water and oil based on the difference in specific gravity. , the oil is typically removed through a separate discharge nozzle and disposed of.
しかして、上記処理に使用される液分離装置即
ちスキミング装置の従来の構造では、原水が収容
された円筒タンクの浮屋根中央に付設されたスキ
ム口からすくい込ませ、更にすくい取られた油分
は、揚降度を可変とした揚降式接続チユーブを介
して油分の排出ノズルに導かれるように形成され
ている。 However, in the conventional structure of the liquid separation device, that is, the skimming device used for the above treatment, the oil is skimmed through a skim opening attached to the center of the floating roof of a cylindrical tank containing raw water, and the oil that is skimmed is , is formed so as to be guided to the oil discharge nozzle via a lift type connecting tube whose lifting degree is variable.
しかして、このような構造方式による従来の液
分離装置の油分取出し作動においては、液面中央
付近の1ケ所だけからしか油分がすくい取られな
いことから、タンク液面全体に亘り均等にかつ効
率よく油分を分離することができないという問題
があつた。 However, in the oil extraction operation of conventional liquid separators with this type of structure, oil is scooped up only from one location near the center of the liquid surface, so oil is scooped out evenly and efficiently over the entire liquid surface of the tank. There was often a problem that the oil could not be separated.
また、特に日本は地震国であり、地震時におい
て、分離タンク内部の液はスロツシング現象を起
こして液面が揺動するが、液面にある浮屋根は、
液の動きと同じ動きをする。したがつて、この
時、浮屋根はスロツシング現象により強い変形や
曲げが加えられて浮屋根に曲げ応力等の応力の増
加があり、浮屋根が破損するおそれがある。 In addition, Japan in particular is an earthquake-prone country, and during an earthquake, the liquid inside the separation tank causes a sloshing phenomenon, causing the liquid level to fluctuate.
It moves in the same way as the liquid moves. Therefore, at this time, the floating roof is strongly deformed and bent due to the sloshing phenomenon, causing an increase in stress such as bending stress on the floating roof, which may cause damage to the floating roof.
本考案は、上記問題点を解消するためになされ
たものであつて、すなわち、本考案の目的は、比
重の違いにより層化された上層の軽質液を効率良
く補集分離すると共に、既設タンクの改造や新設
において実施化が容易な液分離装置を提供するこ
とにある。 The present invention was devised to solve the above-mentioned problems. In other words, the purpose of the present invention is to efficiently collect and separate the light liquid in the upper layer that is stratified due to the difference in specific gravity, and to The object of the present invention is to provide a liquid separation device that is easy to implement in remodeling or new installation.
以下、図示の一実施例に基づいて本考案を説明
する。 Hereinafter, the present invention will be explained based on an illustrated embodiment.
バラスト水の処理工程に設置された実施例の液
分離装置は、第1図ないし第4図に示すように、
固定屋根付きで、かつ、浮屋根Fを有しているタ
ンク1に設けられている。同タンク1の側壁裾部
の一箇所(第2図の右方部)には、処理原水が送
込まれる送入ノズル2が水平に固設されていて、
同送入ノズル2の内方端は、下向きに湾曲成形さ
れると共に、その下端の開口部の周囲には、多数
の孔3aを開けた格子板より成る整流器3が水平
に取付けられている。 The liquid separation device of the embodiment installed in the ballast water treatment process is as shown in Figs. 1 to 4.
It is provided in a tank 1 having a fixed roof and a floating roof F. At one location at the bottom of the side wall of the tank 1 (right side in Figure 2), an inlet nozzle 2 through which treated raw water is sent is fixed horizontally.
The inner end of the inlet nozzle 2 is curved downward, and a rectifier 3 made of a lattice plate with a number of holes 3a is installed horizontally around the opening at the lower end.
また、タンクの側壁裾部の一箇所(第2図の左
方部)に、水分排出ノズル4が水平に突設される
と共に、同水分排出ノズル4の上方至近の側壁に
は、タンク内に水平に張出した油分排出ノズル5
が固設されている。 In addition, a moisture discharge nozzle 4 is provided horizontally protruding from one location at the bottom of the side wall of the tank (the left side in FIG. 2), and a moisture discharge nozzle 4 is provided on the side wall near the top of the moisture discharge nozzle 4 to prevent water from entering the tank. Horizontally projecting oil discharge nozzle 5
is permanently installed.
次に、タンクの収容液Wの液面WLには、第1
図に示すように、上記浮屋根Fが浮かんでおり、
この浮屋根Fは、たとえば断面梯形の浮輪形のフ
ロート7が浮べられていて、同フロート7の内空
は、仕切7aによつて複数区画の防水隔室に形成
されており、かつ該フロート7の中央の空間部に
は、平板状の屋根板8が展設された構造があげら
れる。 Next, at the liquid level WL of the liquid W stored in the tank, there is a first
As shown in the figure, the floating roof F is floating,
This floating roof F has a floating ring-shaped float 7 having a trapezoidal cross section, for example, and the inner space of the float 7 is formed into a plurality of waterproof compartments by partitions 7a. An example is a structure in which a flat roof plate 8 is extended in the central space.
しかして、同屋根板8の下面の中心部には、本
考案に係る分離装置の円筒形の集収器9が固定さ
れていて、同集収器9の底板には、集収器9の内
部9aに通じるスイベル継手10が取付けられて
いる。 A cylindrical collector 9 of the separation device according to the present invention is fixed to the center of the lower surface of the roof plate 8, and the bottom plate of the collector 9 has an inner part 9a of the collector 9. A leading swivel joint 10 is attached.
更に、屋根板8の下面には、複数のブラケツト
11を介して複数本(図示では5本)のスキム管
12が放射状に取付けられていて、各スキム管1
2には、長手方向に沿つて多数のスキム口12a
が穿開されると共に、各スキム管内孔の求心側
は、緩衝用の可撓ホース13を介し、集収器9の
内部9aに開口している。 Further, a plurality of (five in the figure) skim pipes 12 are radially attached to the lower surface of the roof plate 8 via a plurality of brackets 11, and each skim pipe 1
2 has a large number of skim openings 12a along the longitudinal direction.
are opened, and the centripetal side of each skim tube inner hole opens into the interior 9a of the collector 9 via a flexible hose 13 for buffering.
最後に、集収器9のスイベル継手10と排出ノ
ズル5の内方端に設けられたスイベル継手6との
間は、中間にスイベル継手14が介装されて折曲
自在に連結された上部接続チユーブ15と下部接
続チユーブ16とによつて接続されており、これ
により、フロート7は昇降自在に排出ノズル5に
支持されている。 Finally, an upper connecting tube is formed between the swivel joint 10 of the collector 9 and the swivel joint 6 provided at the inner end of the discharge nozzle 5, with a swivel joint 14 interposed in the middle and connected in a bendable manner. 15 and a lower connecting tube 16, whereby the float 7 is supported by the discharge nozzle 5 so as to be movable up and down.
ここで、上述のように構成された実施例の液分
離装置の作動について述べる。 Here, the operation of the liquid separation device of the embodiment configured as described above will be described.
先ず、処理される原水は、送入ノズル2からタ
ンク1内に送り込まれるが、同送入ノズル2の吐
出口につば状に整流器3が配置されていることか
ら、流入する原水流の脈流、乱流によつて生じる
振動圧は、その大部分が整流器3に吸収され、こ
れにより、既に貯蔵されている収容液W中の成分
層を擾乱させることがない。 First, the raw water to be treated is sent into the tank 1 from the inlet nozzle 2, but since a brim-shaped rectifier 3 is arranged at the outlet of the inlet nozzle 2, the incoming raw water flow is pulsating. Most of the vibration pressure generated by the turbulent flow is absorbed by the rectifier 3, so that the component layer in the stored liquid W that has already been stored is not disturbed.
次に、貯蔵時間が或程度経過すると、静置によ
り収容液Wが下層の水分と上層の油分とに成層化
されるので、その後油分排出ノズル5を開けば、
本考案に係る分離装置の各スキム管12の多数の
スキム口12aから液面WLの全面に亘つて管内
に流入する油分は、上下部接続チユーブ15,1
6と排出ノズル5を経て、外部に取出される。 Next, after a certain amount of storage time has elapsed, the stored liquid W is stratified into a lower layer of water and an upper layer of oil by standing still, so if the oil discharge nozzle 5 is then opened,
The oil flowing into the pipe from the numerous skim ports 12a of each skim pipe 12 of the separator according to the present invention over the entire surface of the liquid surface WL flows through the upper and lower connecting tubes 15, 1.
6 and discharge nozzle 5, and is taken out to the outside.
しかして、フロート7の降下につれ、上層の油
分の全量が排出されて油分排出ノズル5からの排
出液中に水分が検知された時点には、油分排出ノ
ズル5を閉成すると共に水分排出ノズル4を開
き、これにより下層の水分を取出して処分する。 As the float 7 descends, the entire amount of oil in the upper layer is discharged and when moisture is detected in the liquid discharged from the oil discharge nozzle 5, the oil discharge nozzle 5 is closed and the moisture discharge nozzle 4 is closed. The bottom layer of water is removed and disposed of.
このような操作と作動を継続的あるいは繰返し
的に実施することにより、静置状態で液面WL全
般からの高流量のスキミング作動に基づき、極め
て効率良く大量の原水を処分することができる。
すなわち、比重の軽い成分は、放射状の各スキム
管12を介して採取しているので、浮屋根Fの屋
根板8全面において小さい流速で収容液Wに乱れ
を発生させない静置状態で比重の軽い成分のみを
極めて効率的に原水より分離採取できる。 By performing such operations continuously or repeatedly, a large amount of raw water can be disposed of extremely efficiently based on the skimming operation at a high flow rate from the entire liquid level WL in a stationary state.
That is, since components with light specific gravity are collected through each radial skim pipe 12, components with light specific gravity are collected in a stationary state without causing disturbance to the stored liquid W at a small flow rate over the entire surface of the roof plate 8 of the floating roof F. Only the components can be separated and collected from raw water extremely efficiently.
また、浮屋根F屋根板8の下面にブラケツト1
1を介して複数のスキム管12を放射状に固定し
た構造であるので、上述したタンク1に限らず既
存のタンクにも簡単にこの考案の装置を取付るこ
とができ、大型のタンク(数m〜数10m直径)を
用いた静置油水分離が可能となるばかりか、地震
時におけるタンク1の内部のスロツシング現象に
よる曲げ応力をを低下させて、各スキム管12が
浮屋根Fの補強部材としての役目を果たし、浮屋
根Fの耐震強度を増加することができる。 In addition, a bracket 1 is attached to the bottom surface of the floating roof F roof plate 8.
Since the structure is such that a plurality of skim pipes 12 are fixed radially through the skim pipes 1, the device of this invention can be easily installed not only in the tank 1 described above but also in existing tanks. This not only makes it possible to perform stationary oil/water separation using a pipe (with a diameter of several tens of meters), but also reduces the bending stress caused by the sloshing phenomenon inside the tank 1 during an earthquake, allowing each skim pipe 12 to serve as a reinforcing member for the floating roof F. The seismic strength of the floating roof F can be increased.
なお、上述したタンクの構成における整流器3
の形成態様につき、格子板3に替え、第5図およ
び第6図に示すように、タンク1底から浮上つて
設置された伏せコツプ型の整流筒17を用いても
良く、すなわち、原水送入ノズル18の内方端を
整流筒17内に開口させると共に、同整流筒17
の上板に原水送入ノズルの通路面積とほぼ等しい
か、それ以上の総面積を有する多数の整流孔17
aを開口させ、これにより、原水流を緩流化させ
る形状としたものである。またタンク1に取付け
られている固定屋根1aを取り除た様な浮屋根円
筒タンクの浮屋根に本装置を取り付けてもよい。 Note that the rectifier 3 in the tank configuration described above
In place of the lattice plate 3, as shown in FIGS. 5 and 6, a rectifier tube 17 of a rectifying cup type floating upward from the bottom of the tank 1 may be used. The inner end of the nozzle 18 is opened into the rectifying cylinder 17, and the rectifying cylinder 17
A large number of rectifying holes 17 having a total area approximately equal to or larger than the passage area of the raw water feed nozzle are provided on the upper plate.
A is opened, thereby slowing down the flow of raw water. Further, the present device may be attached to the floating roof of a floating roof cylindrical tank such as one in which the fixed roof 1a attached to the tank 1 has been removed.
そのほか、実施例の分離作動は、上記水分と油
分の混合液の場合のほか、比重を異にしかつ相互
間において非作用性の液成分を処理対象した場合
におて、全く同様に有効な作動が得られる。 In addition, the separation operation of the embodiment is equally effective when treating liquid components that have different specific gravities and do not interact with each other, in addition to the above-mentioned mixed liquid of water and oil. is obtained.
本考案の効果は下記の通りである。 The effects of the present invention are as follows.
すなわち、本考案においては、浮屋根の下面に
設けられた収集器に一端が連絡され、かつ多数の
スキム口が設けられた複数のスキム管によつて軽
質液を採集するので、各スキム口においては小さ
い流速によつて軽質液を採取してタンク収容液の
不必要な乱れを防止すると共に、液分離装置全体
としては適性な採取流速(採取時間)を確保する
ことができ、極めて効率よく比重の異なる混合液
を静置層化して軽質液を分離除去できる。 That is, in the present invention, light liquid is collected through a plurality of skim pipes each having one end connected to a collector installed on the underside of the floating roof and having a large number of skim ports. The light liquid is sampled at a low flow rate to prevent unnecessary disturbance of the liquid stored in the tank, and the liquid separation device as a whole can secure an appropriate sampling flow rate (sampling time), and is extremely efficient in determining specific gravity. The light liquid can be separated and removed by statically stratifying a mixture of different liquids.
また、収集器を浮屋根の屋根板下面に設けると
共に、収集器に一端が連絡されたスキム管を屋根
板の下面に沿つて複数のブラケツトを介して該屋
根板に複数取り付ける構造なので、これを取り付
ける工事が簡単にでき、既設タンクの改造や新設
において実施化が極めて簡単にできる。 In addition, the collector is installed on the underside of the roof plate of the floating roof, and a plurality of skim pipes, one end of which is connected to the collector, are attached to the roof plate via a plurality of brackets along the underside of the roof plate. Installation work is easy, and it is extremely easy to implement when modifying existing tanks or building new tanks.
特に、既設の浮屋根タンクに改造工事を行う場
合、タンク自身を改造する部分が極めて少なく、
しかも各スキム管が屋根板の補強部材の役目を果
たし改造工事に伴うタンクの補強工事を不要に
し、改造部分はあらかじめ工場にて製作しておく
ことができるため、改造工事期間を大幅に短縮で
き、現場改造工事が極めて容易に完遂出来る。 In particular, when modifying an existing floating roof tank, there are very few parts to modify the tank itself.
In addition, each skim pipe serves as a reinforcing member for the roof plate, eliminating the need for tank reinforcement work associated with remodeling work, and the remodeled parts can be manufactured in advance at the factory, significantly shortening the remodeling period. , site modification work can be completed extremely easily.
第1図は、本考案の一実施例を示す液分離装置
の正断面図、第2図は、第1図の−線におけ
る平断面図、第3図は、第1図の矢指における
部分平面図、第4図は、第2図の−線におけ
る部分断面図、第5図は、タンクの整流器の平面
図、第6図は、同側断面図である。
WL……液面、1……タンク、2,18……送
入ノズル、4……重成分としての水分排出ノズ
ル、5……軽成分としての油分排出ノズル、7…
…フロート、8……屋根板、9……集収器、12
……スキム管、12a……スキム口、15,16
……接続チユーブ、F……浮屋根。
FIG. 1 is a front sectional view of a liquid separation device showing an embodiment of the present invention, FIG. 2 is a plan sectional view taken along the line - in FIG. 1, and FIG. 3 is a partial plane view taken along the arrow in FIG. 4 is a partial sectional view taken along the - line in FIG. 2, FIG. 5 is a plan view of the rectifier of the tank, and FIG. 6 is a sectional view of the same side. WL...liquid level, 1...tank, 2, 18...feeding nozzle, 4...moisture discharge nozzle as heavy component, 5...oil discharge nozzle as light component, 7...
...Float, 8... Roof plate, 9... Collector, 12
...Skim pipe, 12a ...Skim port, 15, 16
...Connection tube, F...Floating roof.
Claims (1)
部にフロートが形成された浮屋根と、 上記屋根板の下面に設けられた収集器と、 上記収集器に一端が連絡されると共に複数のブ
ラケツトを介し上記屋根板の下面に沿つて上記屋
根板に取り付けられ、かつ長手方向に多数のスキ
ム口が設けられた複数のスキム管と、 上記タンクに設けられた軽質液排出ノズルの内
端と上記収集器とを連絡する接続チユーブであつ
て、かつ昇降度を可変とした昇降式接続チユーブ
と、を具備していることを特徴とする液分離装
置。[Scope of Claim for Utility Model Registration] A floating roof provided in a tank and having a float formed on the outer periphery of a flat roof plate, a collector provided on the lower surface of the roof plate, and one end of the collector A plurality of skim pipes are connected to each other and are attached to the roof plate along the lower surface of the roof plate via a plurality of brackets, and are provided with a number of skim ports in the longitudinal direction, and a light pipe provided in the tank. A liquid separation device comprising: a connecting tube that connects the inner end of a liquid discharge nozzle and the collector, and an elevating type connecting tube whose degree of elevation is variable.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3537681U JPS6327830Y2 (en) | 1981-03-16 | 1981-03-16 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3537681U JPS6327830Y2 (en) | 1981-03-16 | 1981-03-16 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS57148403U JPS57148403U (en) | 1982-09-17 |
JPS6327830Y2 true JPS6327830Y2 (en) | 1988-07-27 |
Family
ID=29832638
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3537681U Expired JPS6327830Y2 (en) | 1981-03-16 | 1981-03-16 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6327830Y2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0235671Y2 (en) * | 1985-07-24 | 1990-09-27 | ||
JP2006151854A (en) * | 2004-11-29 | 2006-06-15 | Mitsubishi Gas Chem Co Inc | Method for producing glycidyl methacrylate |
-
1981
- 1981-03-16 JP JP3537681U patent/JPS6327830Y2/ja not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS57148403U (en) | 1982-09-17 |
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