JPH0457784A - Carrying method of plastic fluid and apparatus therefor - Google Patents
Carrying method of plastic fluid and apparatus thereforInfo
- Publication number
- JPH0457784A JPH0457784A JP2166622A JP16662290A JPH0457784A JP H0457784 A JPH0457784 A JP H0457784A JP 2166622 A JP2166622 A JP 2166622A JP 16662290 A JP16662290 A JP 16662290A JP H0457784 A JPH0457784 A JP H0457784A
- Authority
- JP
- Japan
- Prior art keywords
- plastic fluid
- fluid
- storage tank
- thixotropic
- pump
- 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.)
- Pending
Links
- 239000012530 fluid Substances 0.000 title claims abstract description 63
- 239000004033 plastic Substances 0.000 title claims abstract description 55
- 229920003023 plastic Polymers 0.000 title claims abstract description 55
- 238000000034 method Methods 0.000 title claims description 9
- 230000009974 thixotropic effect Effects 0.000 claims abstract description 20
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 238000007664 blowing Methods 0.000 claims abstract description 7
- 238000003860 storage Methods 0.000 claims description 29
- 238000003756 stirring Methods 0.000 claims description 13
- 238000007599 discharging Methods 0.000 claims description 3
- 239000002245 particle Substances 0.000 abstract description 6
- 238000013019 agitation Methods 0.000 abstract 1
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 12
- 239000000725 suspension Substances 0.000 description 12
- 229910000019 calcium carbonate Inorganic materials 0.000 description 6
- 238000010008 shearing Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 2
- 229940069428 antacid Drugs 0.000 description 1
- 239000003159 antacid agent Substances 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 229940079920 digestives acid preparations Drugs 0.000 description 1
- 239000002612 dispersion medium Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- -1 organic synthesis Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000000606 toothpaste Substances 0.000 description 1
- 229940034610 toothpaste Drugs 0.000 description 1
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明はチクソトロピー性の塑性流体の搬出方法およ
びその装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method and apparatus for discharging a thixotropic plastic fluid.
[従来の技術〕
従来、貯留槽内に収容されているニュートン流体、例え
ば重油等を外部に搬出する場合には、全体は比較的均質
に混ざり合うために、荷役液粘度を低下させるためにヒ
ーティングしながら共液撹拌を撹拌用のポンプや撹拌羽
根を有する撹拌機を用いて回流や対流を発生した後に搬
出していた。[Prior Art] Conventionally, when transporting Newtonian fluid, such as heavy oil, stored in a storage tank to the outside, heating is used to reduce the viscosity of the cargo handling fluid in order to mix the fluid relatively homogeneously. While pumping, the liquid was stirred using a stirring pump or a stirrer with stirring blades to generate circulation or convection before being transported out.
ところがある種類の懸濁液はニュートン流体の特性とは
異なり、チクソトロピー(thixotropy)性を
有することが知られている。すなわち、チクソロドビー
性とは懸濁液中に分散する粒子間の牽引力により懸濁液
の内部に連続的な構造が造られ、この構造が剪断によっ
て破壊される時にはじめて流動を起こすが、その後静置
すると一旦、剪断によって破壊された構造が再び形成さ
れて固定化(もとの構造に復元)する物性をいう。However, it is known that some types of suspensions have thixotropic properties, which are different from the properties of Newtonian fluids. In other words, thixorhodobic property means that a continuous structure is created inside the suspension due to the traction force between the particles dispersed in the suspension, and flow occurs only when this structure is broken by shearing, but after that, when it is left still This is a physical property in which the structure that was once destroyed by shearing is re-formed and fixed (restored to its original structure).
このようなチクソトロピー性の塑性流体の一つに炭酸カ
ルシウムの懸濁液がある。One such thixotropic plastic fluid is a suspension of calcium carbonate.
この炭酸カルシウムの用途は、ゴム、プラスチックス、
ペイント、顔料、製紙、肥料、歯磨き粉、酸中前や制酸
剤等の医薬品、有機合成、化粧品等その需要は増加の一
途を辿っている。そして現状においては搬送には液体状
態にすると、懸濁液のチクソロドビー性を有して流動化
が容易には行えないため、吸込口からの液の流入が途切
れることがあった。This calcium carbonate is used in rubber, plastics,
Demand continues to increase for paints, pigments, paper manufacturing, fertilizers, toothpaste, pharmaceuticals such as acid preparations and antacids, organic synthesis, cosmetics, etc. At present, if the liquid is used for transportation, the liquid cannot be easily fluidized due to the thixolodobic properties of the suspension, so that the inflow of the liquid from the suction port may be interrupted.
このため、粉末状態または固形状態により搬送を行って
いるのが実情である。従って現状においては輸送や貯蔵
に多くの時間と設備費、管理費等の費用を費やしていた
。For this reason, the actual situation is that the material is transported in a powder or solid state. Therefore, at present, a lot of time, equipment costs, management costs, etc. are spent on transportation and storage.
上記の如くチクソトロピー性を有する塑性流体の搬送に
ついてはその特性から剪断により構造の破壊を行なわな
ければならず、仮にニュートン流体について使用されて
いた従来の共液撹拌手段を採用する場合には設備費が甚
大になり、また剪断により塑性流体の構造を破壊して流
動性を持たせるのには不充分であり、吸引口からの吸引
が途切れがちで円滑に効率良く行えなかった。また液の
多様化に対応できずに時代の要請に対応することができ
なかった。As mentioned above, when transporting a plastic fluid with thixotropy, its structure must be destroyed by shearing due to its characteristics, and if the conventional co-liquid stirring means used for Newtonian fluids were to be adopted, the equipment cost would be high. Moreover, the shearing was insufficient to destroy the structure of the plastic fluid and give it fluidity, and the suction from the suction port tended to be interrupted, making it impossible to perform it smoothly and efficiently. Furthermore, they were unable to respond to the demands of the times because they were unable to respond to the diversification of liquids.
このためこの発明は、チクソトロピー性の塑性流体につ
いて吸引口からの吸引が途切れることなく効率良く多量
の搬送が行なえるとともに設備費、管理費等の費用がか
からず、さらには需要に応して液の多様化にも適したチ
クソトロピー性の塑性流体の搬出方法およびその装置を
提供することを目的とする。For this reason, the present invention is capable of efficiently transporting a large amount of thixotropic plastic fluid without interrupting the suction from the suction port, without incurring equipment costs, management costs, etc. It is an object of the present invention to provide a method and device for conveying a thixotropic plastic fluid suitable for diversification of liquids.
この発明は上記目的を達成するためになされたものであ
り、このうち1の発明は貯留槽内に収容したチクソトロ
ピー性の塑性流体を、該貯留槽内に階層配置した吹出口
から上下方向に段階毎に兵法を吹出すことによって全体
を兵法撹拌する工程と、撹拌後に前記吹出口に近接して
設けた排出管部から流動化した塑性流体を搬出する工程
とから成るという手段を採用した。The present invention has been made to achieve the above object, and one of the inventions is to step up and down a thixotropic plastic fluid contained in a storage tank from blow-off ports arranged in layers in the storage tank. We adopted a method consisting of a step of agitating the entire body by blowing out tactile fluid at each time, and a step of carrying out the fluidized plastic fluid from a discharge pipe provided close to the outlet after stirring.
また他の発明はチクソトロピー性の塑性流体を収容する
貯留槽と、該貯留槽内に階層配置された撹拌用の吹出口
と、駆動源としてのポンプと、該ポンプに接続され前記
吹出口に近接して前記貯留槽内に階層配置される吸込口
と、貯留槽内に設けられた排出管部とから成り、前記塑
性流体を前記吹出口からの兵法撹拌により撹拌した後に
排出管部から塑性流体を搬出するという手段を採用した
。Further, another invention provides a storage tank containing a thixotropic plastic fluid, a stirring outlet arranged hierarchically in the storage tank, a pump as a driving source, and a pump connected to the pump and close to the outlet. The plastic fluid is made up of a suction port arranged hierarchically in the storage tank, and a discharge pipe part provided in the storage tank, and after the plastic fluid is stirred by tactical stirring from the outlet, the plastic fluid is discharged from the discharge pipe part. We adopted the method of transporting the
貯留槽内に収容されたチクソトロピー性を有する塑性流
体を貯留槽内から外部に搬送するのには貯留槽内に階層
配置された吹出口から兵法を吹出して段階毎に貯留槽内
のチクソトロピー性の塑性流体を兵法撹拌して剪断によ
り粒子間結合により結合力に起因する構造を破壊した後
に流動化し各吹出口に近接する排出管部からポンプにて
吸引して搬出する。In order to transport the thixotropic plastic fluid contained in the storage tank to the outside, the thixotropic plastic fluid inside the storage tank is blown out from the blow-off ports arranged in layers in the storage tank, and the thixotropic plastic fluid inside the storage tank is transported step by step. After the plastic fluid is mechanically stirred and sheared to destroy the structure caused by the bonding force due to interparticle bonds, it is fluidized and is sucked out by a pump from a discharge pipe close to each outlet.
以下、図面に従ってこの発明を海上輸送用の船舶に適用
した場合を一実施例として説明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS An example in which the present invention is applied to a ship for marine transportation will be described below with reference to the drawings.
1は船舶2の甲板3の下部に適宜数設置された貯留槽と
しての船舶であり、この船舶1内にはチクソトロピー性
の塑性流体aが収容されている(図においては1つの船
舶lのみが表示されている)。1 is a ship serving as a storage tank in which an appropriate number of tanks are installed at the lower part of the deck 3 of a ship 2, and a thixotropic plastic fluid a is stored in this ship 1 (in the figure, only one ship l is displayed).
4a、4b、4c、4d、4e、4f、4g4h、4i
、4jは前記船舶1内に適宜間隔毎に対向するように側
壁1a、laの上下方向に沿って階層配置される多数の
吹出口であり、この吹出口4a、 4b、 4c、 4
d、 4e、 4f、 4g。4a, 4b, 4c, 4d, 4e, 4f, 4g4h, 4i
, 4j are a large number of air outlets arranged in layers along the vertical direction of the side walls 1a, la so as to face each other at appropriate intervals in the vessel 1, and these air outlets 4a, 4b, 4c, 4
d, 4e, 4f, 4g.
4h、4i、4jから船舶1へ循環した塑性流体aが順
次、上方から下方に向かって上下方向に吹出すことによ
り、船舶1内に収容されている塑性流体aは段階毎に兵
法撹拌されることによる剪断により、その懸濁液中の粒
子間結合を断切り、構造を破壊して流動化するとともに
経時変化により再び固定化するのを防止する。By sequentially blowing out the plastic fluid a circulated from 4h, 4i, and 4j to the ship 1 in the vertical direction from above to the bottom, the plastic fluid a housed in the ship 1 is stirred step by step. The resulting shearing breaks the interparticle bonds in the suspension, destroys the structure and fluidizes it, and prevents it from becoming immobilized again due to changes over time.
前記塑性流体aとしてはこの実施例においては炭酸カル
シウムの懸濁液を使用しているが、これに限るものでは
ない。Although a suspension of calcium carbonate is used as the plastic fluid a in this embodiment, the plastic fluid a is not limited to this.
5a、 5b、 5c、 5d、 5e、
5f、 5g。5a, 5b, 5c, 5d, 5e,
5f, 5g.
5h、si、sjは前記吹出口4a、4b、4c。5h, si, and sj are the air outlet ports 4a, 4b, and 4c.
4d、4e、4f、4g、4h、4i、4jに近接して
僅かに上方位置に前記側壁1aに沿って階層配置された
多数の吸込口であり、この吸込口5a、5b、5c、5
d、5e、5f、5g、5h。4d, 4e, 4f, 4g, 4h, 4i, and 4j, and are arranged in layers along the side wall 1a at positions slightly above the suction ports 5a, 5b, 5c, 5.
d, 5e, 5f, 5g, 5h.
5i、5j内に例えば上方から段階毎に共液撹拌後の塑
性流体aは吸込まれることにより循環されて前記吹出口
4a、4b、4c、4d、4e、4f、4g、4h、4
i、4jから船舶1内への吹出用として使用の途に供す
る。The plastic fluid a after co-liquid stirring is sucked and circulated into the blow-off ports 4a, 4b, 4c, 4d, 4e, 4f, 4g, 4h, 4 into the blow-off ports 4a, 4b, 4c, 4d, 4e, 4f, 4g, 4h, 4.
It is used for blowing air from i and 4j into the ship 1.
塑性流体aを船舶1から循環して吹出口4a。The plastic fluid a is circulated from the ship 1 to the outlet 4a.
4b、4c、4d、4e、4f、4g、4h、4i、4
jからの吹出しを行うのには各吸込口5a。4b, 4c, 4d, 4e, 4f, 4g, 4h, 4i, 4
Each suction port 5a is used to blow air from the air outlet.
5b、5c、5d、5e、5f、5g、5h、5i、5
jが集約された一次側の管部6の途中に設けたバルブ7
を先ず開き、その後駆動源としてのポンプPにより吸引
し、次いで2次側の管部8の途中に設けられたバルブ9
と前記吹出口4a、4b、4c、4d、4e、4f、4
g、4h、4i。5b, 5c, 5d, 5e, 5f, 5g, 5h, 5i, 5
A valve 7 provided in the middle of the primary side pipe section 6 where j is concentrated
is first opened, then sucked by the pump P as a driving source, and then the valve 9 provided in the middle of the secondary side pipe section 8 is opened.
and the air outlet 4a, 4b, 4c, 4d, 4e, 4f, 4
g, 4h, 4i.
4jに集約される管部工0に接続されるバルブ11を開
くことにより、兵法としての塑性流体aを循環して吹出
口4 a、 4 b、 4 c、 4 d+
4 e。By opening the valve 11 connected to the pipework 0 integrated in 4j, the plastic fluid a is circulated and the air outlet 4a, 4b, 4c, 4d+
4 e.
4f、4g、4h、4i、4jから例えば上方から下方
に向かって段階毎に吹出すようになっている。この場合
、上方から下方に向かって段階毎に塑性流体aを撹拌す
るのはその濃度が薄く、また比重が軽く、粒子の沈澱度
が少ないとともに分子結合力が弱い上澄液の方が下方部
よりもチクソトロピー性の度合いが少なく流動性に冨む
からである。From 4f, 4g, 4h, 4i, and 4j, the air is blown out in stages, for example, from above to below. In this case, if the plastic fluid a is stirred step by step from the top to the bottom, the concentration of the plastic fluid a is lower, the specific gravity is lighter, the degree of sedimentation of particles is less, and the molecular bonding force is weaker. This is because it has a lower degree of thixotropy and more fluidity.
前記管部8の後端には図示しないマニホールドが接続さ
れていて塑性流体aの排出管路を形成している。A manifold (not shown) is connected to the rear end of the pipe portion 8 to form a discharge pipe for the plastic fluid a.
12は船舶1内の底部の適宜位置に少なくとも前記吹出
口4jに近接するように設けられたウェル部であり、こ
のウェル部12の上部の一端に排出管部13の一端が配
置されている。排出管部13の他端はバルブ14を介し
てポンプPに接続されている。Reference numeral 12 denotes a well section provided at a suitable position on the bottom of the vessel 1 so as to be close to at least the air outlet 4j, and one end of the discharge pipe section 13 is disposed at one end of the upper part of the well section 12. The other end of the discharge pipe section 13 is connected to the pump P via a valve 14.
前記ポンプPは、経済的な配慮から船舶を駆動するため
のエンジンEの駆動を利用して回転駆動するようになっ
ている。15は隔壁である。For economic reasons, the pump P is driven to rotate by using the engine E for driving the ship. 15 is a partition wall.
この発明の一実施例は以上の如き構成からなり、以下作
用を工程毎に説明する。One embodiment of the present invention has the above structure, and the operation will be explained step by step below.
(貯留工程)
先ず、船舶1内にチクソトロピー性を有する塑性流体a
としての炭酸カルシウムの懸濁液を供給して貯留するの
には図示していない配管を通して陸上の出荷ポンプから
供給を受けて貯留する。このように貯留槽1内に塑性流
体aを収容することにより、積地から揚地までの海上輸
送に供する。(Storage process) First, a plastic fluid a having thixotropy is placed inside the ship 1.
In order to supply and store a suspension of calcium carbonate, it is supplied from a shipping pump on land through piping (not shown) and stored. By storing the plastic fluid a in the storage tank 1 in this manner, it is used for marine transportation from the loading port to the unloading port.
(撹拌工程)
その後揚地に至り、輸送中に船舶1の底部に沈澱した炭
酸カルシウムの懸濁液を排出し易くするためには静置に
よって再び固定化した塑性流体aを撹拌して流動化する
必要がある。(Stirring process) After that, the plastic fluid a, which has been fixed again by standing still, is stirred and fluidized to make it easier to discharge the calcium carbonate suspension that settled at the bottom of the ship 1 during transportation. There is a need to.
これには先ずバルブ7.9を開き、次いでポンプPを駆
動することにより例えば粒子間結合力が弱く、流動性に
冨んだ貯留槽1の上部を占める塑性流体aを吸込口5a
、5b、5c、5d、5e。To do this, first open the valve 7.9 and then drive the pump P to draw the plastic fluid a, which occupies the upper part of the storage tank 1, which has weak interparticle bonding force and is rich in fluidity, into the suction port 5a.
, 5b, 5c, 5d, 5e.
5f、5g、5h、5i、5jのうちの何れがら吸込ん
で管部6,8を経て搬送する。次いでバルブ11を開い
て吹出口4a、4b、4c、4d4e、4f、4g、4
h、4i、4jの全部または何れから塑性流体aを循環
して貯留槽1内へ吹出すことにより、最もチクソトロピ
ー性に乏しい上方側の塑性流体aから兵法撹拌すること
により繁雑なバルブ操作をすることなく貯留槽1内の塑
性流体aを粒子の種類、形状、濃度等に応じて上下方向
に段階的に撹拌する。このようにして貯留槽1内のチク
ソトロピー性を有する塑性流体aを貯留槽1内において
全体的に撹拌することにより、流動性に冨ませる。Any one of 5f, 5g, 5h, 5i, and 5j is sucked in and conveyed through pipe portions 6 and 8. Next, open the valve 11 and open the air outlets 4a, 4b, 4c, 4d4e, 4f, 4g, 4.
By circulating the plastic fluid a from all or any of h, 4i, and 4j and blowing it out into the storage tank 1, complicated valve operations are performed by tactically stirring the plastic fluid a from the upper side, which has the least thixotropy. The plastic fluid a in the storage tank 1 is stirred in stages in the vertical direction according to the type, shape, concentration, etc. of the particles. In this manner, the plastic fluid a having thixotropy in the storage tank 1 is stirred as a whole within the storage tank 1, thereby increasing its fluidity.
(搬送工程)
而して充分に流動性を有するようになったら貯留槽1の
下部の塑性流体aをポンプPの駆動力により吸引し排出
管部13.8を通じて排出する。(Transporting process) When the plastic fluid a has sufficient fluidity, the plastic fluid a in the lower part of the storage tank 1 is sucked by the driving force of the pump P and discharged through the discharge pipe section 13.8.
なお上記実施例においては貯留槽1内に吸込口5a、5
b、5c、5d、5e、5f、5g、5h、5i、5j
を一例に階層、配置し、また吹出口4a、 4b、 4
c、 4d、 4e、 4f、 4g。In the above embodiment, there are suction ports 5a, 5 in the storage tank 1.
b, 5c, 5d, 5e, 5f, 5g, 5h, 5i, 5j
For example, the hierarchy and arrangement are as follows, and the air outlets 4a, 4b, 4
c, 4d, 4e, 4f, 4g.
4h、4i、4jを対向配置するようにしたがその設置
個数および配列は任意であり、塑性流体aとしてのチク
ソロドビー性を決定する要因、例えば分散質としての粒
子の種類、形状、粒度分布、濃度、分散媒の種類によっ
て任意に選択する。また上記実施例においてはチクソト
ロピー性の塑性流体aとして炭酸カルシウムの懸濁液を
代表例として説明に供したが、これに限ることなく、そ
の他の懸濁液でもよいことはいうまでもない。4h, 4i, and 4j are arranged facing each other, but the number and arrangement of the installed pieces are arbitrary. Factors that determine the thixolodby property of the plastic fluid a, such as the type, shape, particle size distribution, and concentration of particles as dispersoids. , arbitrarily selected depending on the type of dispersion medium. Furthermore, in the above embodiments, a suspension of calcium carbonate was used as a representative example of the thixotropic plastic fluid a, but the present invention is not limited to this, and it goes without saying that other suspensions may be used.
また上記実施例のバルブ7.9,11.14は手動に限
らずに電磁弁等を用いれば電気的制御により吹出、吸込
、搬送等の操作を必要に応じて自動的に制御することが
できる。Further, the valves 7.9, 11.14 in the above embodiments are not limited to manual operation, but can be electrically controlled by using electromagnetic valves or the like to automatically control operations such as blowing, suction, and conveyance as necessary. .
さらに上記実施例においては船舶1に設置する場合を代
表的な実施例として説明したけれども、地上設備におい
ても本発明は適用できることはいうまでもない。Further, although the above embodiment has been described as a typical example in which the device is installed on a ship 1, it goes without saying that the present invention can also be applied to ground equipment.
以上のようにこの発明は、兵法撹拌を採用したことによ
り、チクソトロピー性の塑性流体について貯留槽におけ
る吸引口からの吸引が途切れることなく効率良く行え、
以て多量の搬送が行なえるとともに設備費、管理費等の
費用が低層になり、さらには需要に応して懸濁液の多様
化にも対応できる。As described above, by employing tactical stirring, this invention enables efficient and continuous suction of thixotropic plastic fluid from the suction port in the storage tank.
This makes it possible to transport a large amount, lower costs such as equipment costs and management costs, and furthermore, it is possible to handle the diversification of suspensions according to demand.
第1図はこの発明の一実施例を示す断面図である。
1・・・船舶、2・・・船舶、4a、 4b、 4
c、 4−d4e、4f、4g、4h、4i、4j−
吹出口、5a、5b、5c、5d、5e、5f、5g、
5h、5i、5j・・・吸込口、6,8,10.12・
・・管部、7,9,11.14・・・パルプ、13・・
・排出管部、a・・・塑性流体、E・・・エンジン。FIG. 1 is a sectional view showing an embodiment of the present invention. 1... Ship, 2... Ship, 4a, 4b, 4
c, 4-d4e, 4f, 4g, 4h, 4i, 4j-
Air outlet, 5a, 5b, 5c, 5d, 5e, 5f, 5g,
5h, 5i, 5j... Suction port, 6, 8, 10.12.
・・Pipe part, 7, 9, 11. 14・・Pulp, 13・・
- Discharge pipe section, a... plastic fluid, E... engine.
Claims (2)
を、該貯留槽内に階層配置した吹出口から上下方向に段
階毎に共液を吹出すことによって全体を共液撹拌する工
程と、撹拌後に前記吹出口に近接して設けた排出管部か
ら流動化した塑性流体を搬出する工程とから成るチクソ
トロピー性の塑性流体の搬出方法。(1) A step of stirring the entire thixotropic plastic fluid contained in a storage tank by blowing out the co-liquid in stages in the vertical direction from blow-off ports arranged in layers in the storage tank; A method for discharging a thixotropic plastic fluid, which comprises the step of subsequently discharging the fluidized plastic fluid from a discharge pipe provided close to the outlet.
、該貯留槽内に階層配置された撹拌用の吹出口と、駆動
源としてのポンプと、該ポンプに接続され前記吹出口に
近接して前記貯留槽内に階層配置される吸込口と、貯留
槽内に設けられた排出管部とから成り、前記塑性流体を
前記吹出口からの共液撹拌により撹拌した後に排出管部
から塑性流体を搬出することを特徴とするチクソトロピ
ー性の塑性流体の搬送装置。(2) A storage tank containing a thixotropic plastic fluid, a stirring outlet arranged hierarchically in the storage tank, a pump as a driving source, and a pump connected to the pump and close to the outlet. It consists of a suction port arranged hierarchically in the storage tank and a discharge pipe section provided in the storage tank, and after the plastic fluid is stirred by co-liquid stirring from the outlet port, the plastic fluid is discharged from the discharge pipe section. A device for transporting a thixotropic plastic fluid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2166622A JPH0457784A (en) | 1990-06-27 | 1990-06-27 | Carrying method of plastic fluid and apparatus therefor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2166622A JPH0457784A (en) | 1990-06-27 | 1990-06-27 | Carrying method of plastic fluid and apparatus therefor |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0457784A true JPH0457784A (en) | 1992-02-25 |
Family
ID=15834708
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2166622A Pending JPH0457784A (en) | 1990-06-27 | 1990-06-27 | Carrying method of plastic fluid and apparatus therefor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0457784A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59145683A (en) * | 1983-02-10 | 1984-08-21 | Nippon Kokan Kk <Nkk> | Uniform discharger of slop tank liquid for chemical tanker |
-
1990
- 1990-06-27 JP JP2166622A patent/JPH0457784A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59145683A (en) * | 1983-02-10 | 1984-08-21 | Nippon Kokan Kk <Nkk> | Uniform discharger of slop tank liquid for chemical tanker |
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