JPH10245571A - Process and apparatus for separating and recovering sand-contaminated heavy oil - Google Patents

Process and apparatus for separating and recovering sand-contaminated heavy oil

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Publication number
JPH10245571A
JPH10245571A JP8988397A JP8988397A JPH10245571A JP H10245571 A JPH10245571 A JP H10245571A JP 8988397 A JP8988397 A JP 8988397A JP 8988397 A JP8988397 A JP 8988397A JP H10245571 A JPH10245571 A JP H10245571A
Authority
JP
Japan
Prior art keywords
sand
heavy oil
oil
tank
water
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
Application number
JP8988397A
Other languages
Japanese (ja)
Inventor
Shinichi Miyae
伸一 宮江
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP8988397A priority Critical patent/JPH10245571A/en
Publication of JPH10245571A publication Critical patent/JPH10245571A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide a process and an apparatus for completely separating heavy oil lumps drifted on shore and recovered together with sand into sand and heavy oil. SOLUTION: Sand-contaminated heavy oil lumps are introduced into a basket tumbled in a heavy liquid of saturated brine filled into an oil/sand separation tank 1 and heated to high temperature, crushed into finer easily meltable lumps. The finer lumps are separated into sand and heave oil, which floats owing to the difference between their specific gravities, and only the supernatant heavy oil is separated and recovered from a discharge trough 10. On the other hand, the sand having a larger specific gravity and settled to the sand collection pit 13 on the bottom a sand separation tank 1 is pulled up from the tank with a sand pull up bucket conveyor 12 and heated again to remove the residual oil, and continuously discharged from a sand discharge trough by means of a sand discharge trough conveyor 16. The heavy oil lumps are introduced into the basket 4 through a net conveyor 24. Sand not contaminated with heavy oil is screened by vertically tumbling the conveyor 24, and only the heavy oil lumps can be introduced. Therefore, a large amount of sand-contaminated heavy oil lumps can be continuously treated without extra energy consumption.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は,タンカー事故や石
油備蓄施設などから漏出して海岸に漂着した重油を回収
する際,砂や異物とともに回収された汚染重油を砂や異
物と重油とを効率よく分離して回収する方法と装置に関
するものである.
BACKGROUND OF THE INVENTION The present invention relates to a method for recovering contaminated heavy oil collected along with sand and foreign matter from sand, foreign matter and heavy oil when recovering heavy oil that has leaked from a tanker accident or an oil storage facility and drifted to the shore. It relates to a method and apparatus for separating and recovering well.

【0002】[0002]

【従来の技術】現在,砂浜に漂着した重油は波浪によっ
て波打ち際に点在あるいは帯状に打ち上げられており,
その上に漂砂が覆い重油と砂が幾層にも重なっており人
力による回収に頼らざるを得ないのが現状である.した
がってドラム缶に回収された重油には砂質分が多く(成
分分析では砂質70%,水分20%,油質6〜7%),
焼却処分の際にも困難をきたしている.砂混じりの汚染
重油の分離回収では,水面上の浮遊油を吸い上げて遠心
分離する実験(ケビン・コスナー社など)が行われたが
重油の粘度が高く分離が困難であった.またMJP(望
月式混気ジェットポンプ)による分離回収実験が行なわ
れたが分離された砂に油分が残るなどの問題があった.
一方,土木機械で集積した油質分5%の大量の砂の山を
処理する手立てはなく,油質分5%未満の砂の埋め立て
処分が検討されており土壌や地下水の汚染などの環境破
壊が危惧されている.
2. Description of the Related Art At present, heavy oil that has drifted on a sandy beach has been scattered or swept up by waves when it is hit by waves.
On top of that, drifting sand covers heavy oil and sand in multiple layers, and at present it has to rely on manual recovery. Therefore, the heavy oil recovered in the drum has a large amount of sand (70% sand, 20% water, 6-7% oil) in the component analysis.
Difficulties also arise during incineration. In the separation and recovery of contaminated heavy oil mixed with sand, an experiment was conducted in which the floating oil on the water surface was sucked up and centrifuged (eg, Kevin Costner), but the viscosity of heavy oil was high and separation was difficult. Separation and recovery experiments using MJP (Mochizuki-type air-mixing jet pump) were also conducted, but there was a problem such as oil remaining in the separated sand.
On the other hand, there is no way to treat a large pile of sand with an oil content of 5% accumulated by civil engineering machinery, and landfill disposal of sand with an oil content of less than 5% is being considered, and environmental destruction such as soil and groundwater contamination is being considered. Is feared.

【0003】[0003]

【発明が解決しようとする課題】人力(ボランティア)
によって回収された重油塊には砂や海草などの異物が混
在しているが,これから重油と砂を分離する技術はまだ
確立されていない.汚染重油は回収現場で完全に分離し
て重油だけドラム缶に回収すれば減量されて輸送量が減
るとともに焼却以外の再利用の用途も可能であり,一方
分離回収された砂は海中へ投入すれば僅かな残留油分は
石油分解バクテリアによって処理されて浄化され,減少
する傾向にある砂浜の保全にもなる.本発明は,砂など
の異物が混入する回収重油を重油と砂とに完全に分離す
る技術を提供するものである.
[Problems to be solved by the invention] Human power (volunteer)
The foreign bodies such as sand and seaweed are mixed in the heavy oil mass recovered by the method, but the technology to separate heavy oil and sand from it has not been established yet. If the contaminated heavy oil is completely separated at the recovery site and only the heavy oil is collected in drums, the weight will be reduced and the transport volume will be reduced, and it will be possible to reuse it other than incineration. On the other hand, if the separated and collected sand is put into the sea, The small amount of residual oil is treated and purified by petroleum-degrading bacteria, which also preserves the declining beaches. The present invention provides a technique for completely separating recovered heavy oil mixed with foreign substances such as sand into heavy oil and sand.

【0004】[0004]

【課題を解決するための手段】本発明は砂などで汚染さ
れた重油塊を砂と重油に分離するものである.砂浜に漂
着した揮発成分の乏しい重油は比重が大きく粘着性が極
めて高いため,砂や海草などが多量に混在する回収重油
を分離するためには,高温度に熱した水槽中で重油塊を
撹拌,破砕して融解させ,比重差によって分離して回収
するものである.請求項2に記載の発明は,比重の大き
な重油塊を高濃度の塩水の重液との比重差によって浮上
分離を容易にし回収率の改善を目的としたものである.
請求項3に記載の発明は,高温水槽の水面下に設けた金
網製のバスケットに回収重油塊を投入して,バスケット
を回転または揺動させて重油塊を破砕微細化して融解し
易くするとともに,該バスケット内に残留した海草や異
物を除去するものである.バスケットから高温水槽中に
溶出した重油は粘度が低下して容易に砂と分離し高濃度
塩水との比重差によって水面上に浮上するので回収升の
堰から越流させて回収する.請求項4に記載の発明は,
塩水よりも比重の大きな砂は分離水槽の底部へ沈殿する
ので水槽の底面を水中における砂の安息角(約30゜)
以上の傾斜として水槽の最深部の集砂升に砂を集めてバ
ケットコンベヤー,ジェットコンベヤー,気泡ポンプな
どで油砂分離水槽の水面よりも高い水面の二次処理槽内
へ水とともに砂を引揚げてバーナーで再加熱し,撹拌洗
浄することで砂中に残留する油分を完全に分離除去する
ものである.再洗浄された砂は二次処理槽内からトラフ
コンベヤーなどによって引揚げて回収する.一方,二次
処理槽内の水面上に浮上した油膜は水とともに油砂分離
槽内へ返送される.請求項5に記載の発明は,土木機械
で集積された重油含有率の少ない膨大な量の砂には油に
汚染されていない砂が多く,この余剰な砂を機械的な篩
で除去して砂混じりの重油塊だけを分離水槽へ投入する
ことで槽内の湯温の低下を防止するとともに加熱するエ
ネルギーの節減を謀るものである.油で汚染されていな
い乾燥した砂は目の細かい篩で容易に篩分けができるの
で,ネットコンベヤーの駆動用のチェーンに上下方向の
衝撃的な振動を間欠的に与えることで連続的に余剰な砂
を篩分けながら分離水槽に重油塊だけを投入することが
できる.請求項6に記載の発明は,請求項5装置で余剰
の砂を篩分ける際に砂が湿っていたり多量の水分を含む
場合には目の細かな篩では篩分けは困難である.しかし
水中では砂が分散するので容易に篩分けができ,さらに
水に濡れた篩には重油が付着しにくい性質を利用するも
のである.そこでネットコンベヤーの下端を海水を満た
した水槽中に沈めておき砂混じりの重油塊を海水中のネ
ットコンベヤーの上に投入して余剰の砂を洗い流すもの
である.この方法を海岸で行う場合には重油塊が漏出し
ないように細かい金網で周囲を囲うが,海水に融解した
重油が海面上に浮遊するので周辺をオイルフェンスで囲
い,別途に用意された浮遊油回収装置によって回収する
必要がある.
SUMMARY OF THE INVENTION The present invention separates heavy oil lumps contaminated with sand and the like into sand and heavy oil. Since heavy oil with few volatile components drifted on the sandy beach has a large specific gravity and extremely high tackiness, in order to separate recovered heavy oil containing a large amount of sand and seaweed, a heavy oil mass is stirred in a water tank heated to a high temperature. It is crushed, melted, and separated and recovered according to the difference in specific gravity. The second object of the present invention is to facilitate the flotation separation of heavy oil lumps having a large specific gravity with the heavy liquid of high-concentration salt water to improve the recovery rate.
According to a third aspect of the present invention, the collected heavy oil lumps are put into a wire mesh basket provided below the surface of the high-temperature water tank, and the basket is rotated or rocked to crush and refine the heavy oil lumps to facilitate melting. , For removing seaweed and foreign matter remaining in the basket. The heavy oil eluted from the basket into the high-temperature water tank has a reduced viscosity and easily separates from sand, and floats on the water surface due to the difference in specific gravity with high-concentration salt water. The invention described in claim 4 is:
Sand with a higher specific gravity than salt water settles at the bottom of the separation tank, so the bottom of the tank is set at the angle of repose of sand in water (about 30 °).
With the above inclination, the sand is collected in the sand collecting tank at the deepest part of the water tank, and the sand and the sand are lifted by a bucket conveyor, jet conveyor, bubble pump, etc. into the secondary treatment tank on the surface of the water higher than the surface of the oil and sand separation tank. The oil remaining in the sand is completely separated and removed by reheating with a burner and washing with stirring. The rewashed sand is recovered from the secondary treatment tank by using a trough conveyor. On the other hand, the oil film floating on the water surface in the secondary treatment tank is returned to the oil and sand separation tank together with water. According to a fifth aspect of the present invention, the enormous amount of sand with a low content of heavy oil accumulated in the civil engineering machinery contains a large amount of sand not contaminated with oil, and the excess sand is removed by a mechanical sieve. By putting only heavy oil lumps mixed with sand into the separation water tank, it is possible to prevent the temperature of the hot water in the tank from dropping and to save energy for heating. Dry sand that has not been contaminated with oil can be easily sieved with a fine sieve, so that continuous excess surplus can be obtained by intermittently applying a shocking vibration in the vertical direction to the driving chain of the net conveyor. Only heavy oil lumps can be put into the separation tank while sieving the sand. According to the sixth aspect of the present invention, when the excess sand is sieved by the apparatus according to the fifth aspect, if the sand is wet or contains a large amount of water, it is difficult to sieve with a fine sieve. However, since the sand is dispersed in water, it can be easily sieved, and heavy oil does not easily adhere to the wet sieve. Therefore, the lower end of the net conveyor is submerged in a tank filled with seawater, and heavy oil lumps mixed with sand are poured onto the net conveyor in seawater to wash away excess sand. When this method is used on the shore, the surrounding area is surrounded by a fine wire mesh to prevent heavy oil lumps from leaking. However, since the heavy oil dissolved in seawater floats on the sea surface, surround the area with an oil fence and use a separately prepared floating oil. It must be collected by a collecting device.

【0005】[0005]

【作用】砂浜に漂着した重油を回収した砂や異物を含む
重油塊は揮発成分がなく比重が1.002〜1.007
と大きく水中に沈む.さらに比重が約2.6の砂粒が混
在しているために比重が1.03の海水にも沈むので,
海水に塩を加えて比重が1.2の飽和塩水の重液を用い
て比重差によって浮上分離する.また,回収重油の粘度
は非常に大きく常温では容易に溶解しないので飽和塩水
を70℃〜80℃の高温度に過熱して回収重油を軟化さ
せて撹拌することで砂と分離し易くする必要がある.ま
た,回収重油は大きな塊りとなっており高温塩水中にそ
のまま投入しても沈んでしまうので,油砂分離槽水面の
上層部に設置した目の粗い金網製のバスケットの中に投
入してバスケットを回転または揺動させて重油塊を破
砕,微細化することで融解し易くするとともに水槽の底
部に重油塊が沈降するのを防止している.なお,該バス
ケットは砂混じりの回収重油中に混在する海草や異物を
除去することも目的としている.高温度で軟化した重油
は流動性がよくなり飽和塩水よりも比重が小さいので容
易に浮上分離するが,十分に融解せずに砂を含んだまま
浮上する重油塊もあるので上澄液だけが流下するような
仕切板を設け,その後方に上澄液が回収升へ素通りする
のを防止するために水面上部に仕切板を設けて該仕切板
の下部から再浮上した重油を回収升に越流させて排出管
からドラム缶などに回収する.一方,油砂分離槽で沈殿
した砂は底面の傾斜に沿って集砂升に集積されるのでバ
ケットコンベヤーなどで油砂分離槽より僅かに水位の高
い二次処理槽へ引き上げて再加熱して残留油分を完全に
浮遊分離させてトラフコンベヤーなどで引き上げて回収
する.二次処理槽の水面には薄い油膜が浮くから余剰の
水とともに油砂分離槽へ落差によって返送する.
[Function] A heavy oil mass containing sand and foreign matter from which heavy oil collected on a sandy beach is recovered has no volatile components and a specific gravity of 1.002 to 1.007.
It sinks greatly in the water. In addition, since sand particles with a specific gravity of about 2.6 are mixed, they sink in seawater with a specific gravity of 1.03.
Salt is added to seawater and floated and separated according to the difference in specific gravity using a saturated saline solution with a specific gravity of 1.2. In addition, the viscosity of the recovered heavy oil is so large that it does not easily dissolve at room temperature. Therefore, it is necessary to heat saturated brine to a high temperature of 70 ° C to 80 ° C to soften the recovered heavy oil and stir it so that it can be easily separated from sand. is there. Also, since the recovered heavy oil is a large lump and sinks when poured directly into high-temperature salt water, it is poured into a coarse-meshed wire mesh basket installed in the upper layer of the surface of the oil and sand separation tank. By rotating or rocking the basket, the heavy oil lumps are crushed and refined to make it easier to melt and prevent the heavy oil lumps from settling at the bottom of the water tank. The basket is also intended to remove seagrass and foreign substances contained in the recovered heavy oil mixed with sand. Heavy oil softened at high temperature has good fluidity and has a lower specific gravity than saturated brine, so it easily floats and separates. However, some heavy oil lumps that float with sand without melting sufficiently, so only the supernatant is used. Provide a partition plate that flows down, and a partition plate is provided above the water surface to prevent the supernatant liquid from passing through to the recovery tank, and the heavy oil re-emerged from the lower part of the partition plate is transferred to the recovery tank. Make it flow and collect it from a discharge pipe into a drum. On the other hand, the sand that has settled in the oil / sand separation tank is accumulated in the sand collecting pit along the slope of the bottom, so it is pulled up to a secondary treatment tank with a slightly higher water level than the oil / sand separation tank by a bucket conveyor or the like, and reheated. The residual oil is completely suspended and separated, and then lifted and collected with a trough conveyor. Since a thin oil film floats on the water surface of the secondary treatment tank, it is returned to the oil and sand separation tank together with excess water by head.

【0006】[0006]

【発明の実施の形態】添付図面を用いて本発明の実施の
形態を説明する.実施例として図1に油砂分離槽の上面
図を,図2に側面図を示す.図1の油砂分離槽1の底面
2は砂が集砂升13に自然に流下するように砂の安息角
(約30゜)以上の傾斜がつけられている.その底面2
の下方から加熱バーナー3で油砂分離槽を加熱するよう
になっており,油砂分離槽1には高温度の飽和塩水が満
たされている.その一端の水面部に目の粗い金網製のバ
スケット4が設けられており,ベルトコンベヤーまたは
ネットコンベヤー24によって砂混じりの重油塊が該バ
スケットに連続的に投入される.図3にA−A´断面を
示す.バスケット4をクランク5と揺動レバー6によっ
て揺動運動させるとバスケット4内の重油塊は破砕し細
分化されて融解し重油と砂とが容易に分離し易くなる.
また重油塊とともに回収された海草や塵芥はバスケット
4内に残留するのでこれらを回収除去することができ
る.高温度に融解した重油は流動性がよくなり水面上に
浮上し,分離された砂は底部に沈殿して集砂升13へ流
下する.図4(a)に仕切板7を,図4の(b)に仕切
板8を示す.浮上した重油にはまだ砂を含む重油塊も混
在するのでそのまま重油回収升9に流れ込むのを防止す
るために図4(a)に示す仕切板7を設けて水面上の上
澄み部だけを下流へ流し出す.さらにその下流に図4
(b)に示す仕切板8を設けて水面部を遮断して仕切板
8の下部の傾斜した切り欠き部分の下から浮上した重油
を回収升9へ送り込む.図5にB−B´断面を示す.仕
切板8の下から浮遊した重油は回収升9の上縁から越流
させて重油排出口10から流出させ重油排出樋11によ
って集油槽18に回収する.仕切板7,8は油の処理状
況によって適宜上下に調節できるようになっている.
Embodiments of the present invention will be described with reference to the accompanying drawings. As an example, Fig. 1 shows a top view of an oil and sand separation tank, and Fig. 2 shows a side view. The bottom surface 2 of the oil / sand separation tank 1 in FIG. 1 is inclined more than the angle of repose of the sand (about 30 °) so that the sand naturally flows down to the sand collecting pit 13. Its bottom 2
The oil-sand separation tank is heated by a heating burner 3 from below the oil-sand separation tank 1, and the oil-sand separation tank 1 is filled with high-temperature saturated brine. A basket 4 made of a coarse mesh is provided on the water surface at one end, and heavy oil lumps mixed with sand are continuously fed into the basket by a belt conveyor or a net conveyor 24. FIG. 3 shows an AA ′ cross section. When the basket 4 is oscillated by the crank 5 and the swing lever 6, the heavy oil mass in the basket 4 is crushed and fragmented and melted, and the heavy oil and sand are easily separated.
The seaweed and refuse collected together with the heavy oil lumps remain in the basket 4 so that they can be collected and removed. The heavy oil melted at a high temperature has good fluidity and floats on the water surface, and the separated sand precipitates at the bottom and flows down to the sand collecting pit 13. FIG. 4A shows the partition plate 7, and FIG. 4B shows the partition plate 8. Since the heavy oil that has floated still contains heavy oil lumps containing sand, a partition plate 7 shown in FIG. 4A is provided to prevent the heavy oil lumps from flowing directly into the heavy oil recovery box 9 and only the supernatant on the water surface is moved downstream. Pour out. Fig. 4
A partition plate 8 shown in (b) is provided to cut off the water surface portion, and the heavy oil floating from below the inclined cutout portion at the lower portion of the partition plate 8 is sent to the recovery tank 9. FIG. 5 shows a BB ′ cross section. The heavy oil floating from below the partition plate 8 flows over the upper edge of the recovery box 9, flows out of the heavy oil discharge port 10, and is collected in the oil collection tank 18 by the heavy oil discharge gutter 11. The partition plates 7 and 8 can be adjusted up and down as appropriate according to the oil processing situation.

【0007】油砂分離槽1内の砂の処理装置の一例を説
明する.図6にC−C´断面および図7にD−D´断面
を示す.油砂分離槽1の底部斜面2を流下して集砂升1
3に集積した砂は図6に示すバケットコンベヤー12で
油砂分離槽1の水面よりもHだけ高い水位の二次処理槽
14に引き上げられる.二次処理槽14はその底面から
再加熱用バーナー15で加熱されており,砂とともに引
き上げられた水面上には砂に付着した残留油分が分離さ
れて浮上するので上澄みの油を水とともに落差Hを利用
して返送管18によって油砂分離槽1へ返送している.
二次処理槽14で再洗浄されて底部に沈積した砂は図7
に示すトラフコンベヤー16によって砂排出樋17から
排出される.
An example of an apparatus for treating sand in the oil / sand separation tank 1 will be described. FIG. 6 shows a section taken along the line CC ′, and FIG. 7 shows a section taken along the line DD ′. The sand collecting tank 1 flows down the slope 2 at the bottom of the oil and sand separation tank 1
The sand accumulated in 3 is lifted by a bucket conveyor 12 shown in FIG. 6 into a secondary treatment tank 14 having a water level higher than the water level of the oil and sand separation tank 1 by H. The secondary treatment tank 14 is heated from the bottom by a reheating burner 15, and the residual oil adhering to the sand is separated and floats on the surface of the water lifted together with the sand. The oil is returned to the oil and sand separation tank 1 by the return pipe 18 using the above.
The sand re-washed in the secondary treatment tank 14 and deposited on the bottom is shown in FIG.
Are discharged from the sand discharge gutter 17 by the trough conveyor 16 shown in FIG.

【0008】図2の油砂分離槽1の下の加熱部には点検
窓19が設けられており,その上方の壁面には余熱を利
用した清水の湯沸かしタンク20が設置してあり油砂分
離槽への補給水や洗浄に利用できるようにしてある.さ
らに,加熱バーナー3排気は排気孔21から排気筒22
を経て大気中へ放出される.回収した硫黄分の多い重油
などを燃料として使用する際には簡易型の排煙脱硫装置
23を設置する必要がある.
An inspection window 19 is provided in a heating section below the oil and sand separation tank 1 in FIG. 2, and a water tank 20 for fresh water using residual heat is installed on a wall surface above the inspection window. It can be used for replenishing water to the tank and for cleaning. Further, the exhaust of the heating burner 3 is discharged from the exhaust hole 21 to the exhaust pipe 22.
It is released to the atmosphere via. It is necessary to install a simple flue gas desulfurization device 23 when using the recovered heavy fuel oil or the like as fuel.

【0009】油砂分離槽1を効率よく運転するには処理
状態を監視しながら重油塊を定量ずつ連続的に投入する
必要があり,それにはベルトコンベヤーやネットコンベ
ヤーの使用が適している.図8にネットコンベヤー24
による重油塊の供給装置の一例を示す.図示のものはネ
ットコンベヤー24の下部を水槽25中に没した場合の
様子を示しているが,砂の状態によってはその必要がな
い場合もある.ネットコンベヤー24のネット26上に
砂混じりの重油塊を乗せて油砂分離槽1内へ投入する際
に油で汚染されていない砂はネットによって篩い落とさ
れて重油塊だけがバスケット4に投入される.ネット2
6で篩い落とされた砂はE−E´断面に示す遮蔽板27
によってコンベヤー24の両外側に落下させて戻り側の
ネット26´の上部に砂が落ちるのを防止している.図
9はネット26に振動を与える機構の詳細図である.砂
がネット26から落ちにくい場合には図9に示すよう
に,チェンの数ピッチごとにローラ付きのロッド29を
設けたチェンを鋸歯状の突起28を付けたチェンガイド
レール上を走行させることでチェンに上下方向の衝撃的
な振動を与えてネット26から砂を篩い落とし易くして
いる.鋸歯状の突起部28の各間隔 lはチェンのピッ
チpの整数倍に一致しないようにすることで,ネットコ
ンベヤー24の各部分を交互に振動させることができ
る.
In order to operate the oil / sand separation tank 1 efficiently, it is necessary to continuously feed the heavy oil lumps by a constant amount while monitoring the treatment state. For this purpose, a belt conveyor or a net conveyor is suitable. FIG. 8 shows the net conveyor 24.
An example of a device for supplying heavy oil lumps by means of is shown. The figure shows a state in which the lower part of the net conveyor 24 is immersed in the water tank 25, but this may not be necessary depending on the state of the sand. When a heavy oil lump mixed with sand is put on the net 26 of the net conveyor 24 and put into the oil / sand separation tank 1, sand not contaminated with oil is sieved off by the net, and only the heavy oil lump is put into the basket 4. It is. Net 2
The sand sieved in Step 6 is the shielding plate 27 shown in the EE 'section.
This prevents the sand from dropping on the upper side of the return net 26 'by dropping to both outer sides of the conveyor 24. FIG. 9 is a detailed view of a mechanism for applying vibration to the net 26. If the sand is hard to fall from the net 26, as shown in FIG. 9, a chain provided with a rod 29 with a roller at every several pitches of the chain is run on a chain guide rail provided with a serrated protrusion 28. A vertical shock is applied to the chain to facilitate sieving sand from the net 26. By making each interval l of the sawtooth-shaped projections 28 not coincide with an integral multiple of the chain pitch p, each part of the net conveyor 24 can be vibrated alternately.

【0010】[0010]

【発明の効果】海岸に漂着した重油は砂や海草などとと
もに回収されてドラム缶に詰めて処理業者まで輸送して
焼却処理されているが,多量の砂や水分を含んでいるた
め膨大なエネルギーが必要であり処理に困難をきたして
いる.本発明は,揮発成分が気化して高粘度となった重
油塊を高温度に熱した高濃度の塩水中に投入して重油の
粘度を低下させて融解し,比重差によって砂と分離する
ものである.したがって回収される重油は減量され輸送
量が著しく減少するとともに砂や異物を含まず重油成分
だけとなるために以後の処理が容易となる本方式特有の
効果が得られる.また分離回収された砂は単に撹拌分離
する他の方法に比べて加熱処理されるため砂に付着した
重油分が完全に除去されるという特徴的な効果が認めら
れる.処理後の砂には微かに匂いが残るが2〜3日後に
は全く匂いもなくなることが判った.比重差による分離
効率を高めるために重液として飽和塩水を用いるが,分
離処理槽内だけでの完全なクローズドシステムのため外
界の環境に影響を与えることはない.塩水の分析結果で
はCODは20ppm以下であった.また,量的にも油
砂分離槽の容積分だけであるのでそのまま海洋へ戻して
も自然環境には何ら影響を与えない.さらに,重油に汚
染されていない砂をあらかじめ除去するため熱エネルギ
ーの消費量も少なくて済み,砂に混在する海草や塵芥な
どの異物も回収除去するなどの効果も付加される..
According to the present invention, heavy oil that has drifted to the shore is collected together with sand and seaweed, packed in drums, transported to a processing company, and incinerated. However, since it contains a large amount of sand and water, a huge amount of energy is consumed. Necessary and difficult to process. The present invention relates to a method in which a heavy oil mass having a high viscosity due to a volatile component being vaporized is poured into a high-concentration salt water heated to a high temperature to lower the viscosity of the heavy oil and melt, and separated from sand by a difference in specific gravity. . Therefore, the recovered heavy oil is reduced in weight and the amount of transportation is significantly reduced, and since only heavy oil components are contained without sand or foreign substances, the following effects unique to this system can be obtained. Separated and recovered sand is heat-treated compared to other methods of simply stirring and separating, and has the distinctive effect of completely removing heavy oil attached to the sand. It was found that the smell was slightly left on the sand after the treatment, but it disappeared completely after 2-3 days. Saturated salt water is used as a heavy liquid to increase the separation efficiency due to the difference in specific gravity. The salt water analysis showed that the COD was less than 20 ppm. Also, since the quantity is only the capacity of the oil and sand separation tank, returning it to the ocean as it is does not affect the natural environment at all. Furthermore, the removal of sand that is not contaminated with heavy oil in advance reduces the amount of heat energy consumed, and also has the added effect of collecting and removing foreign substances such as seagrass and dust mixed in the sand. .

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

【図1】実施例の油砂分離槽の上面図である.FIG. 1 is a top view of an oil and sand separation tank of an embodiment.

【図2】実施例の油砂分離槽の側面図である.FIG. 2 is a side view of the oil and sand separation tank of the embodiment.

【図3】油砂分離槽内のバスケットを揺動する機構の説
明図である.
FIG. 3 is an explanatory view of a mechanism for swinging a basket in an oil-sand separation tank.

【図4】(a)は上流側仕切板,(b)は下流側仕切板
の説明図である.
FIG. 4 (a) is an explanatory view of an upstream partition plate, and FIG. 4 (b) is an explanatory view of a downstream partition plate.

【図5】重油回収部の断面図である.FIG. 5 is a sectional view of a heavy oil recovery section.

【図6】集砂升から砂引き上げ用バケットコンベヤー部
の断面図である.
FIG. 6 is a cross-sectional view of a bucket conveyor for raising sand from a sand collecting pit.

【図7】二次処理槽からの排砂用トラフコンベヤー部の
断面図である.
FIG. 7 is a cross-sectional view of a trough conveyor for sand removal from a secondary treatment tank.

【図8】油砂分離槽への重油塊投入用のネットコンベヤ
ー部の断面図である.
FIG. 8 is a cross-sectional view of a net conveyor section for putting heavy oil lumps into the oil and sand separation tank.

【図9】投入用ネットコンベヤー部のネットの加振機構
の詳細説明図である.
FIG. 9 is a detailed explanatory diagram of a net vibrating mechanism of a feeding net conveyor section.

【符号の説明】[Explanation of symbols]

1 油砂分離槽 3 加熱用バーナー 4 重油塊破砕用バスケット 5,6 バスケット揺動機構 10 回収重油排出樋 14 砂引上げ用バケットコンベヤー 15 二次処理槽 18 排砂用トラフコンベヤー 19 砂排出樋 21 清水用湯沸かしタンク 25 重油塊投入用ネットコンベヤー 28 ネットコンベヤー加振用鋸歯状ガイドレー
DESCRIPTION OF SYMBOLS 1 Oil-sand separation tank 3 Heating burner 4 Heavy oil chunk crushing basket 5, 6 Basket swinging mechanism 10 Recovery heavy oil discharge gutter 14 Sand pulling bucket conveyor 15 Secondary treatment tank 18 Sand discharge trough conveyor 19 Sand discharge gutter 21 Shimizu Water heater tank 25 Net conveyor for loading heavy oil lumps 28 Serrated guide rail for net conveyor vibration

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 海岸に漂着して砂などで汚染された高粘
度の重油塊を,温水を満たした水槽に投入して撹拌,破
砕することで重油の粘度を低下させて砂と重油とが分離
し易くし,比重差によって砂は水槽の底部に沈降させ,
温水より比重の小さな重油を水槽の上層部に浮上させて
回収する汚染重油の分離回収方法.
1. A high-viscosity heavy oil mass that has drifted ashore and is contaminated with sand or the like is put into a water tank filled with warm water, stirred and crushed to lower the viscosity of the heavy oil and to form sand and heavy oil. The sand is settled at the bottom of the tank due to the specific gravity difference,
A method for separating and recovering contaminated heavy oil, in which heavy oil having a specific gravity lower than that of hot water is floated to the upper part of the tank and collected.
【請求項2】 揮発成分が気化して比重が大きくなった
重油などの分離には,水槽中に重液として高濃度の塩水
を満たして重油との比重差を大きくして浮上分離の効率
を改善することを特徴とする請求項1に記載の汚染重油
の分離回収方法.
2. For separation of heavy oil or the like whose specific gravity has increased due to vaporization of volatile components, a water tank is filled with high-concentration salt water as a heavy liquid to increase the difference in specific gravity from heavy oil to increase the efficiency of flotation separation. The method for separating and recovering contaminated heavy oil according to claim 1, wherein the method is improved.
【請求項3】砂混じりの重油塊を油砂分離水槽内の上層
水面下に没して設置された金網製のバスケットに投入し
て,該バスケットを回転または揺動させて重油塊を細か
く破砕することにより重油塊の融解を促進させて油砂分
離を容易にすることを特徴とする汚染重油の分離回収装
置.
3. A heavy oil mass containing sand is poured into a wire mesh basket placed under the upper surface of the water in an oil / sand separation tank, and the basket is rotated or rocked to finely crush the heavy oil mass. A separation and recovery system for contaminated heavy oil, characterized by promoting the melting of heavy oil lumps and facilitating oil and sand separation.
【請求項4】油砂分離水槽の底部に沈殿した砂をバケッ
トコンベヤーなどによって分離水槽の水面より高い水面
の二次処理槽内に引揚げて再過熱,撹拌洗浄して砂中の
残留油分を除去し,二次処理槽水面に浮上した油膜を水
とともに油砂分離槽へ返送する構造にした回収砂の残留
油分を完全に除去するための二次処理槽を設けたことを
特徴とする油砂分離装置.
4. The sand settled at the bottom of the oil / sand separation tank is lifted by a bucket conveyor or the like into a secondary treatment tank having a water surface higher than the water surface of the separation water tank, reheated and stirred and washed to remove residual oil in the sand. An oil characterized by having a secondary treatment tank for completely removing the residual oil content of the recovered sand, which is configured to remove and return the oil film floating on the water surface of the secondary treatment tank to the oil sand separation tank together with the water Sand separator.
【請求項5】 多量の砂に混在する重油塊は,予め目の
細かい篩で油に汚染されていない余剰な砂を篩い落とし
て砂混じりの重油塊だけを分離回収槽へ投入する.この
操作を連続的に行うためにはネットコンベヤーを用いる
が,ネットコンベヤーの駆動用チェーンに上下方向の衝
撃的な振動を間欠的に与える加振機構を備えたことを特
徴とする砂と重油塊の篩分け分離装置.
5. Heavy oil lumps mixed in a large amount of sand are sieved in advance with excess sand not contaminated with oil through a fine-meshed sieve, and only heavy oil lumps mixed with sand are put into a separation and recovery tank. To perform this operation continuously, a net conveyor is used, but sand and heavy oil lumps are characterized by having a vibration mechanism that intermittently applies vertical shocking vibration to the driving chain of the net conveyor. Sieving separation equipment.
【請求項6】砂に混じった重油塊を分離する方法におい
て,湿った砂や多量の水分を含んだ砂の場合にはネット
コンベヤーの下部を水を満たした水槽または海中に没入
させておき,砂混じりの重油塊を海水中のネットコンベ
ヤー上へ投入して余剰の砂を洗い流すことを特徴とする
請求項4に記載の砂と重油の湿式篩分け分離装置.
6. A method for separating heavy oil lumps mixed with sand, wherein in the case of wet sand or sand containing a large amount of water, the lower part of the net conveyor is immersed in a water tank or sea filled with water, The wet-sieving separation apparatus for sand and heavy oil according to claim 4, wherein the heavy oil lumps mixed with sand are poured onto a net conveyor in seawater to wash away excess sand.
JP8988397A 1997-03-03 1997-03-03 Process and apparatus for separating and recovering sand-contaminated heavy oil Pending JPH10245571A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8988397A JPH10245571A (en) 1997-03-03 1997-03-03 Process and apparatus for separating and recovering sand-contaminated heavy oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8988397A JPH10245571A (en) 1997-03-03 1997-03-03 Process and apparatus for separating and recovering sand-contaminated heavy oil

Publications (1)

Publication Number Publication Date
JPH10245571A true JPH10245571A (en) 1998-09-14

Family

ID=13983172

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8988397A Pending JPH10245571A (en) 1997-03-03 1997-03-03 Process and apparatus for separating and recovering sand-contaminated heavy oil

Country Status (1)

Country Link
JP (1) JPH10245571A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102765825A (en) * 2011-05-06 2012-11-07 上海兰艳实业有限公司 Grease separator
CN116197351A (en) * 2023-02-07 2023-06-02 无锡范尼韦尔工程有限公司 Cleaning device for floating sand barrel impurities and online cleaning method thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102765825A (en) * 2011-05-06 2012-11-07 上海兰艳实业有限公司 Grease separator
CN116197351A (en) * 2023-02-07 2023-06-02 无锡范尼韦尔工程有限公司 Cleaning device for floating sand barrel impurities and online cleaning method thereof

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