JPS6129997B2 - - Google Patents

Info

Publication number
JPS6129997B2
JPS6129997B2 JP14662977A JP14662977A JPS6129997B2 JP S6129997 B2 JPS6129997 B2 JP S6129997B2 JP 14662977 A JP14662977 A JP 14662977A JP 14662977 A JP14662977 A JP 14662977A JP S6129997 B2 JPS6129997 B2 JP S6129997B2
Authority
JP
Japan
Prior art keywords
crude oil
oil
tank
water
residual
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
JP14662977A
Other languages
Japanese (ja)
Other versions
JPS5433502A (en
Inventor
Akio Tsutsui
Kenji Nagao
Tadashi Hayashi
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.)
Taiho Kogyo Co Ltd
Original Assignee
Taiho Kogyo 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 Taiho Kogyo Co Ltd filed Critical Taiho Kogyo Co Ltd
Priority to JP14662977A priority Critical patent/JPS5433502A/en
Publication of JPS5433502A publication Critical patent/JPS5433502A/en
Publication of JPS6129997B2 publication Critical patent/JPS6129997B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は原油タンク等において、底部に残存し
てワツクス成分を多量に含む残油を原油とともに
処理してタンク外に排出し、回収するようにした
ことを特徴とするタンクにおける原油の残油を回
収する方法に関するものである。
[Detailed Description of the Invention] The present invention is characterized in that in a crude oil tank or the like, residual oil remaining at the bottom and containing a large amount of wax components is treated together with the crude oil, discharged outside the tank, and recovered. The present invention relates to a method for recovering residual crude oil in a tank.

周知のように原油タンク等においては長期間の
利用で底部に残油(スラツジ)が沈積する。この
残油はワツクス分を多く含み、固化してタンクの
操作や付帯設備に支障を来すばかりでなく、タン
クの内容積の減少原因となるので、定期的に除去
しなければならない。
As is well known, residual oil (sludge) accumulates at the bottom of crude oil tanks after long-term use. This residual oil contains a large amount of wax and solidifies, which not only interferes with the operation of the tank and associated equipment, but also causes a decrease in the internal volume of the tank, so it must be removed periodically.

従来の残油の除去方法としてはタンク内部から
原油をほとんど排出した後、ホースをタンクの底
部にとどくように挿入し、友油、水、スチームな
どをホースから強く噴射して残油を底部から剥離
し、油水混合状態でタンクから排出するのであ
る。また、タンク内部から原油をほとんど排出し
た後に水や海水を供給し、既設の加熱コイルにス
チームを供給して水を80℃にまで加温し、加温し
て溶解した残油を水面に浮上してポンプアウトす
る方法も採用されている。更に上記以外にも多種
の方法が知られている。
The conventional method for removing residual oil is to drain most of the crude oil from inside the tank, then insert a hose so that it reaches the bottom of the tank, and forcefully spray oil, water, steam, etc. from the hose to remove the remaining oil from the bottom. It is peeled off and discharged from the tank in a mixed state of oil and water. In addition, water or seawater is supplied after most of the crude oil has been discharged from inside the tank, and steam is supplied to the existing heating coil to heat the water to 80℃, causing the heated and dissolved residual oil to float to the surface of the water. A method of pumping out is also adopted. Furthermore, various methods other than those described above are known.

しかしいずれの方法も大規模な原油タンクにお
いては著しい手間と時間を要し、しかも排出され
る残油に多量の水や化学剤が含まれているので油
水分離により精製することができず、廃棄しなけ
ればならない。
However, both methods require considerable time and effort in large-scale crude oil tanks, and the residual oil that is discharged contains large amounts of water and chemical agents, so it cannot be purified by oil-water separation and is discarded. Must.

本発明は原油槽底部に堆積する残油層に流動性
有る原油を存在させた状態で、加温水を原油の上
方で略水平方向に噴射して原油を加温し、加温さ
れた原油と温水の噴射勢とにより残油を流動状態
にするとともに、加温水の噴射勢で原油槽の周辺
部に移動させ、残油を原油と温水との混合状態で
ポンプアウトなどにより排出して油水分離し、回
収するようにしたものであつて、更に回収した残
油にワツクス分散剤を添加したり、希釈油に混合
希釈するものであるから残油を再度使用に供する
ことができる。したがつて経済的に無駄を生じな
いばかりでなく、設置が著しく簡単で、処理時間
を短縮することができる。
In the present invention, while fluid crude oil is present in the residual oil layer deposited at the bottom of the crude oil tank, heated water is injected in a substantially horizontal direction above the crude oil to warm the crude oil, and the heated crude oil and hot water are heated. The residual oil is made into a fluid state by the injection force of the heated water, and is moved to the periphery of the crude oil tank by the injection force of the heated water, and the remaining oil is discharged as a mixture of crude oil and hot water by pumping out, and the oil and water are separated. The residual oil can be used again since it is recovered and a wax dispersant is added to the recovered residual oil or mixed and diluted with diluted oil. Therefore, not only is there no economic waste, the installation is extremely simple and the processing time can be shortened.

次に本発明の回収方法を図面に基いて説明する
と、浮屋根式原油槽1の内部に有るワツクス成分
の多い固化した残油aは一般に底部に沈積固化し
ているので、残油の回収作業時には残油に少量の
流動性ある原油bを存在させる。原油の量は適宜
であるが、加温されたとき少くともすべての残油
を溶解させる程度でなければならない。
Next, the recovery method of the present invention will be explained based on the drawings. The solidified residual oil a containing a large amount of wax inside the floating roof type crude oil tank 1 is generally deposited and solidified at the bottom, so the residual oil recovery process Sometimes a small amount of fluid crude oil b is present in the residual oil. The amount of crude oil is suitable, but it must be sufficient to dissolve at least all the residual oil when heated.

原油槽1の内部側壁に有るマンホール2のフラ
ンジには温水の噴射装置3を設け、該噴射装置3
に連結管4を接続する。連結管4には加温装置5
を設けて三方弁6に接続し、三方弁6には給水管
7と還流管8を接続する。還流管8は他端を原油
槽1の底部からの排出ポンプ9に連結する油水分
離装置10に接続する。そして加温装置5には油
水分離剤を供給する供給管11を接続する。
A hot water injection device 3 is provided on the flange of a manhole 2 on the inner side wall of the crude oil tank 1.
Connect the connecting pipe 4 to. A heating device 5 is installed in the connecting pipe 4.
is provided and connected to the three-way valve 6, and the three-way valve 6 is connected to a water supply pipe 7 and a reflux pipe 8. The reflux pipe 8 is connected at the other end to an oil-water separator 10 which is connected to a discharge pump 9 from the bottom of the crude oil tank 1 . A supply pipe 11 for supplying an oil-water separation agent is connected to the heating device 5.

上記した噴射装置3は原油槽1の内部に温水を
原油の上方で略水平方向に噴射することができ、
また略水平状態のまゝ左右に往復揺動して温水を
扇状域に噴射できる構造である。この噴射装置3
の往復揺動は温水の噴射勢で自動的に揺動させて
もよいし、原油槽の外部から機械的又は手動で操
作しながら揺動させるようにしてもよい。
The injection device 3 described above can inject hot water into the crude oil tank 1 in a substantially horizontal direction above the crude oil,
It also has a structure that allows it to swing back and forth from side to side while remaining in a substantially horizontal position to spray hot water into a fan-shaped area. This injection device 3
The reciprocating swing may be made automatically by the force of hot water jets, or may be made to swing while being mechanically or manually operated from outside the crude oil tank.

このような噴射装置3を原油槽の側壁の数ケ所
(3〜4ケ所)に設置するのであるが、設置は残
油の排出作業を行う時にマンホール2の蓋を開放
し、フランジに取り付けて給水管7を接続すれば
よい。
Such an injection device 3 is installed at several locations (3 to 4 locations) on the side wall of the crude oil tank, and when the residual oil is being discharged, the manhole 2 cover is opened and the injection device 3 is attached to the flange to supply water. Just connect the pipe 7.

このようにしてなる原油槽1の内部の残油を回
収するには、前記したように底部に残油と原油を
存在させたまゝ給水管7から供給される水を加温
装置5で60〜90℃に加温し、また必要に応じて油
水分離剤を添加して連結管4から噴射装置3に供
給する。したがつて複数の噴射装置から同時又は
交互に、或いは連続的若しくは間歇的に温水を原
油の上方に噴射させると、温水は原油槽1の底部
の全域に供給され、シヤワー状となつて流動性あ
る原油層上面に供給されて原油層を加温する。そ
して加温された原油層の熱と温水の噴射勢とによ
り、下層のワツクス成分の多い残油層は溶解し、
流動性が与えられる。残油層が流動状態になると
上面に供給される温水は残油層にまで達し、その
過程で残油層がさらに加温されるので溶解が促進
され、原油と残油とが混合して水層上に浮上す
る。
In order to recover the residual oil inside the crude oil tank 1 formed in this manner, water supplied from the water supply pipe 7 is heated to 60 to The mixture is heated to 90° C., an oil-water separation agent is added as required, and the mixture is supplied to the injection device 3 through the connecting pipe 4. Therefore, when hot water is injected above the crude oil simultaneously or alternately, continuously or intermittently from a plurality of injection devices, the hot water is supplied to the entire bottom of the crude oil tank 1, forming a shower shape and increasing the fluidity. It is supplied to the top of a certain crude oil layer and warms the crude oil layer. Then, due to the heat of the heated crude oil layer and the injection force of hot water, the residual oil layer with a lot of wax components in the lower layer is dissolved.
Provides liquidity. When the residual oil layer becomes fluid, the hot water supplied to the top reaches the residual oil layer, and in the process, the residual oil layer is further heated, promoting dissolution, and the crude oil and residual oil mix and flow onto the water layer. surface.

上記の様に残油が溶解若しくは一部溶解して原
油槽1の底部より離脱し、流動状態になると側方
から噴射される噴射装置の温水噴射勢によつて原
油槽の底部中央に滞流することがなく、強制的に
原油槽の周辺部に移動する。そして周辺部に移動
した残油は原油及び温水とともにポンプ9でポン
プアウトし、加温状態のまゝAPI、CPI等の油水
分離装置10に導く。この装置10で分離された
温水は還流管8から三方弁6を伝わつて加温装置
5で所定温度まで温められ、連結管4から原油槽
1に還流される。
As mentioned above, the residual oil dissolves or partially dissolves and separates from the bottom of the crude oil tank 1, and when it becomes fluid, it remains in the center of the bottom of the crude oil tank by the hot water injection force of the injection device that is injected from the side. without being forced to move to the vicinity of the crude oil tank. The residual oil that has moved to the surrounding area is pumped out by a pump 9 together with crude oil and hot water, and is guided in a heated state to an oil-water separator 10 such as API or CPI. The hot water separated by this device 10 is passed through the three-way valve 6 from the reflux pipe 8, heated to a predetermined temperature by the heating device 5, and then refluxed to the crude oil tank 1 from the connecting pipe 4.

油水分離装置10で分離された残油成分を含む
油成分は遠心分離器等で更に水分を除去するか或
いはしないで、他の流動性ある油類を希釈油とし
て混合装置12で混合してからまた上記油成分に
希釈油を混合するとワツクス成分が再析出するこ
とがあるので、分散剤を添加してワツクス成分の
再析出防止を図つてもよい。
The oil component containing the residual oil component separated in the oil-water separator 10 is further removed with a centrifuge or the like, or without water, and mixed with other fluid oils as diluent oil in the mixer 12. Further, when a diluent oil is mixed with the above-mentioned oil component, the wax component may re-precipitate, so a dispersant may be added to prevent the wax component from re-precipitating.

以上で明らかなように本発明によれば原油槽の
底部に残油と流動性ある原油とを存在させた状態
で、加温水を原油の上方で略水平方向に噴射して
原油を加温し、加温された原油と温水の噴射勢と
により残油を流動状態にするとともに、加温水の
噴射勢で原油槽の周辺部に移動させて排出するよ
うにしたので、残油が著しく効率よく流動状態と
なる。また温水を原油の上方から略水平方向に噴
射するので、溶解した残油と原油とが温水ととも
に原油槽の周辺部に直ちに移動することになり、
残油を回収する時間と手間とを著しく軽減するこ
とができる。したがつて原油槽内の残油を回収す
る場合にだけ温水噴射装置を例えばマンホールに
設置すればよいから既設の原油タンクでも実施す
ることができ、特に大型の原油タンクにおいて有
効である。
As is clear from the above, according to the present invention, while residual oil and fluid crude oil are present at the bottom of a crude oil tank, heated water is injected in a substantially horizontal direction above the crude oil to heat the crude oil. The residual oil is made into a fluid state by the heated crude oil and the injection force of hot water, and the residual oil is moved to the periphery of the crude oil tank and discharged by the injection force of the heated water, so the residual oil is removed extremely efficiently. Becomes a fluid state. In addition, since hot water is injected from above the crude oil in a substantially horizontal direction, the dissolved residual oil and crude oil immediately move to the periphery of the crude oil tank together with the hot water.
The time and effort required to recover residual oil can be significantly reduced. Therefore, since it is only necessary to install a hot water injection device in a manhole, for example, when recovering residual oil in a crude oil tank, it can be carried out even in an existing crude oil tank, and is particularly effective in a large crude oil tank.

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

図面は本発明の実施例を示す概略図である。 The drawings are schematic illustrations of embodiments of the invention.

Claims (1)

【特許請求の範囲】[Claims] 1 原油槽の底部に残油と流動性有る原油とを存
在させた状態で、噴射装置により温水を原油の上
方で略水平方向に噴射させて原油の上面に供給
し、温水の供給によつて加温された原油と温水の
噴射勢とにより残油を流動状態にし、流動状態に
なつた残油を噴射装置の温水噴射勢により原油槽
の周辺部に移動させて油水混合状態で原油槽の外
部に排出するようにしたことを特徴とする原油槽
底部の残油を回収する方法。
1 With residual oil and fluid crude oil present at the bottom of the crude oil tank, hot water is injected approximately horizontally above the crude oil using an injection device to supply it to the upper surface of the crude oil. The residual oil is made into a fluid state by the heated crude oil and the hot water injection force, and the fluidized residual oil is moved to the periphery of the crude oil tank by the hot water injection force of the injection device, and the oil and water are mixed in the crude oil tank. A method for recovering residual oil at the bottom of a crude oil tank, characterized by discharging it to the outside.
JP14662977A 1977-12-08 1977-12-08 Recovery of residual oil in bottom of crude oil tank Granted JPS5433502A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14662977A JPS5433502A (en) 1977-12-08 1977-12-08 Recovery of residual oil in bottom of crude oil tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14662977A JPS5433502A (en) 1977-12-08 1977-12-08 Recovery of residual oil in bottom of crude oil tank

Publications (2)

Publication Number Publication Date
JPS5433502A JPS5433502A (en) 1979-03-12
JPS6129997B2 true JPS6129997B2 (en) 1986-07-10

Family

ID=15412046

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14662977A Granted JPS5433502A (en) 1977-12-08 1977-12-08 Recovery of residual oil in bottom of crude oil tank

Country Status (1)

Country Link
JP (1) JPS5433502A (en)

Also Published As

Publication number Publication date
JPS5433502A (en) 1979-03-12

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