JPH0322918B2 - - Google Patents
Info
- Publication number
- JPH0322918B2 JPH0322918B2 JP57157417A JP15741782A JPH0322918B2 JP H0322918 B2 JPH0322918 B2 JP H0322918B2 JP 57157417 A JP57157417 A JP 57157417A JP 15741782 A JP15741782 A JP 15741782A JP H0322918 B2 JPH0322918 B2 JP H0322918B2
- Authority
- JP
- Japan
- Prior art keywords
- oil
- specific gravity
- suspension
- surfactant
- spilled
- 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 - Lifetime
Links
- 230000005484 gravity Effects 0.000 claims description 21
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 10
- JFNLZVQOOSMTJK-KNVOCYPGSA-N norbornene Chemical compound C1[C@@H]2CC[C@H]1C=C2 JFNLZVQOOSMTJK-KNVOCYPGSA-N 0.000 claims description 10
- 239000004094 surface-active agent Substances 0.000 claims description 10
- 239000002245 particle Substances 0.000 claims description 9
- 239000007864 aqueous solution Substances 0.000 claims description 7
- 229920000642 polymer Polymers 0.000 claims description 7
- 239000000843 powder Substances 0.000 claims description 5
- 229920000098 polyolefin Polymers 0.000 claims description 4
- 239000000344 soap Substances 0.000 claims description 4
- 239000002563 ionic surfactant Substances 0.000 claims description 3
- 239000000693 micelle Substances 0.000 claims description 3
- 239000008233 hard water Substances 0.000 claims description 2
- 230000001112 coagulating effect Effects 0.000 claims 1
- 239000003921 oil Substances 0.000 description 25
- 239000000725 suspension Substances 0.000 description 17
- 238000000034 method Methods 0.000 description 13
- 239000003795 chemical substances by application Substances 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 8
- 239000002585 base Substances 0.000 description 7
- 239000003350 kerosene Substances 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 239000013535 sea water Substances 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- 239000002904 solvent Substances 0.000 description 6
- 239000000243 solution Substances 0.000 description 5
- 239000003349 gelling agent Substances 0.000 description 4
- 239000012263 liquid product Substances 0.000 description 4
- 239000002075 main ingredient Substances 0.000 description 4
- -1 polyethylene Polymers 0.000 description 4
- 238000005507 spraying Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000004743 Polypropylene Substances 0.000 description 3
- 230000002776 aggregation Effects 0.000 description 3
- 239000012153 distilled water Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005189 flocculation Methods 0.000 description 3
- 230000016615 flocculation Effects 0.000 description 3
- 239000000295 fuel oil Substances 0.000 description 3
- 229920001155 polypropylene Polymers 0.000 description 3
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- 239000002270 dispersing agent Substances 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000004945 emulsification Methods 0.000 description 2
- 229930195729 fatty acid Natural products 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 238000001879 gelation Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000003305 oil spill Substances 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 231100000419 toxicity Toxicity 0.000 description 2
- 230000001988 toxicity Effects 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical class OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 150000003862 amino acid derivatives Chemical class 0.000 description 1
- 239000003945 anionic surfactant Substances 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 231100000053 low toxicity Toxicity 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 238000009372 pisciculture Methods 0.000 description 1
- 229920000636 poly(norbornene) polymer Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
【発明の詳細な説明】
本発明は、使用簡便にして効率が高く、しかも
水棲動植物に殆んど害を及ぼさない流出油凝集剤
に係り、更に詳しくは真比重が1以下のオレフイ
ン重合体、2−ノルボーネン重合体等の親油性粉
末を、該粉末と真比重が近似する親水性有機溶剤
水溶液に懸濁せしめるか、該処理中に臨界ミセル
濃度に近い濃度の界面活性剤および/またはアル
カリ石鹸等の硬水耐性のイオン性界面活性剤を存
在せしめて成ることを特徴とする流出油凝集剤に
関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a spilled oil flocculant that is easy to use, highly efficient, and causes little harm to aquatic animals and plants, and more specifically, an olefin polymer having a true specific gravity of 1 or less; A lipophilic powder such as a 2-norbornene polymer is suspended in an aqueous solution of a hydrophilic organic solvent whose true specific gravity is similar to that of the powder, or a surfactant and/or alkali soap at a concentration close to the critical micelle concentration is added during the treatment. This invention relates to a spilled oil flocculant characterized in that it contains a hard water resistant ionic surfactant such as.
近年、タンカー事故、油槽所、工場事故等によ
り海上、陸水系に流出した原油、重油、軽質油等
は沿岸汚染の原因となるのみならず養殖魚業等に
も重大な損失を及ぼす所謂公害の大きな一因をな
している。 In recent years, crude oil, heavy oil, light oil, etc. that have spilled into the sea and land water systems due to tanker accidents, oil depots, factory accidents, etc. are causing so-called pollution that not only causes coastal pollution but also causes serious losses to the fish farming industry. It's a big factor.
これら流出油の処理清掃法としてオイルフエン
スにより囲み、これを機械的に吸い上げる単純な
操作以外に、ポリオレフイン等の重合物により構
成された所謂吸着マツトを散設し、これに吸着せ
しめて回収する方法、乳化剤を主剤とした所謂流
出油処理剤を散布してこれを乳化分散拡散せしめ
る方法、アミノ酸誘導体やソルビトール誘導体、
2−ノルボーネン重合体等の凝油、ゲル化剤を散
布して該流出油を凝油、ゲル化物として回収する
方法が周知である。 In addition to the simple operation of enclosing oil in an oil fence and mechanically sucking up the spilled oil, there is also a method of collecting the spilled oil by installing so-called adsorption mats made of polymers such as polyolefin and allowing the oil to be absorbed by these mats. , a method of spraying a so-called spilled oil treatment agent containing an emulsifier as a main ingredient to emulsify and disperse it, amino acid derivatives and sorbitol derivatives,
A well-known method is to spray a coagulated oil such as a 2-norbornene polymer or a gelling agent and recover the spilled oil as a coagulated oil or a gelled product.
これらの方法はいずれも一定の条件下では有効
もしくは唯一の可能性ある方法として油流出事故
の状況に応じて選別的に実施されている方法であ
るが、主剤が液状製品である流出油処理剤を除
き、他はいずれも主剤が固形もしくは粉末である
ため広域に広がつた油面に対する散設、散布には
困難を併なうものである。その解決策として主剤
固形成分を溶解可能な親油性溶剤に主剤を溶解せ
しめ、ポンプ散布等の可能な液状製品としたり、
界面活性剤を使用して水に分散せしめた製品とす
るか、あるいはまた親油性溶剤と界面活性剤を併
用して主剤を溶解分散せしめた液状製品とするこ
とが従来公知の方法であつた。 All of these methods are effective or the only possible method under certain conditions and are selectively implemented depending on the situation of the oil spill accident, but oil spill dispersants whose main agent is a liquid product With the exception of , all of the others have solid or powdered base agents, making it difficult to spread and spread over a wide area of oil. As a solution to this problem, the base agent is dissolved in a lipophilic solvent that can dissolve the solid component of the base agent to create a liquid product that can be sprayed with a pump.
Conventionally known methods include using a surfactant to create a product that is dispersed in water, or using a combination of a lipophilic solvent and a surfactant to create a liquid product that dissolves and disperses the main ingredient.
しかしながら、主剤固形成分を親油性溶剤に溶
解せしめて液状製品とする方法は、使用する溶剤
の毒性が二次公害を惹起する一因となるなどの課
題が残されており、それを避けるためには高価な
低毒性特殊溶剤を使用するため、実用上流出油の
数倍以上の高価な処理剤とならざるを得ない欠点
がある。また、界面活性剤で主剤固形粉末を水に
懸濁せしめる方法は、懸濁液として安定な製品で
あることは殊更海水や陸水に散布した場合の拡散
乳化性も大で、流出油の乳化分散剤としての目的
には合致するものの、凝集ゲル化を目的とする製
品においては主剤のロスが極めて大きく、製品の
単価は安くつくが効率が著しく減少するので総合
的経済性は極めて不利益となる上、主剤粒子の表
面上で界面活性剤の親油基が主剤粒子側に、親水
基が水相側に配列するため肝心の流出油との親和
性が悪化し、凝集、ゲル化時間も著しく大となる
欠点を有している。 However, the method of dissolving the base solid component in a lipophilic solvent to make a liquid product still has problems, such as the toxicity of the solvent used, which causes secondary pollution. Since this method uses an expensive, low-toxicity special solvent, it has the disadvantage that in practice, the treatment agent must be several times more expensive than the spilled oil. In addition, the method of suspending the main solid powder in water with a surfactant is a stable product as a suspension, which also has high dispersion and emulsification properties when sprayed on seawater or land water, and emulsification of spilled oil. Although it meets the purpose as a dispersant, in products intended for agglomeration and gelation, the loss of the main agent is extremely large, and although the unit price of the product is low, the efficiency is significantly reduced, so the overall economic efficiency is extremely disadvantageous. Moreover, on the surface of the main agent particles, the lipophilic groups of the surfactant are arranged on the main agent particle side and the hydrophilic groups are arranged on the aqueous phase side, which deteriorates the essential affinity with spilled oil and increases the aggregation and gelation time. It has significant drawbacks.
本発明は前述の凝集、ゲル化剤の液状化方法に
残された課題を解決し、安定にして使用簡便かつ
高効率で速効性、しかも低公害で安価な流出油の
凝集、ゲル化剤を提供するものである。 The present invention solves the problems remaining in the above-mentioned methods for liquefying flocculation and gelling agents, and provides a stable, easy-to-use, highly efficient, fast-acting, low-pollution, and inexpensive flocculation and gelling agent for spilled oil. This is what we provide.
即ち、本発明の特色とするところはポリエチレ
ン、ポリプロピレン等のポリオレフイン、2−ノ
ルボーネン重合体等の真比重が1以下の凝油性、
吸油性物質を可及的微粒子とする一方、メタノー
ル、エタノール、プロパノール、イソプロパノー
ル、ブタノール等の低級アルコール類その他比重
が1以下の親水性溶剤に水を加え、当該微粒状主
剤と同一比重の溶液を作り、これに前記微粒状主
剤を加えてホモミキサー等にて充分に撹拌を行な
つて液状懸濁型凝集、ゲル化剤としたところにあ
る。 That is, the characteristics of the present invention are that polyolefins such as polyethylene and polypropylene, oil-curing properties such as 2-norbornene polymers having a true specific gravity of 1 or less;
While making the oil-absorbing substance into as fine particles as possible, water is added to lower alcohols such as methanol, ethanol, propanol, isopropanol, butanol, and other hydrophilic solvents with a specific gravity of 1 or less to form a solution with the same specific gravity as the fine particulate base material. The above-mentioned fine particulate main ingredient is added to this, and the mixture is thoroughly stirred using a homomixer or the like to form a liquid suspension-type aggregation and gelling agent.
主成分としては油に対する凝集性能が特にすぐ
れている2−ノルボーネン重合物(分子量200万
以上)が好ましい。市販の2−ノルボーネン重合
物〔ポリ(1.3−チクロペンチレンビニレン)〕は
すでに1mm以下の粒度であるからそのまま使用し
ても良いが、更に粒度の小さいものを得るためこ
れを再粉砕してもよい。 The main component is preferably a 2-norbornene polymer (molecular weight of 2 million or more), which has particularly excellent flocculation performance against oil. Commercially available 2-norbornene polymer [poly(1,3-cyclopentylene vinylene)] already has a particle size of 1 mm or less, so it can be used as is, but it can also be re-pulverized to obtain an even smaller particle size. good.
アルコール類としては毒性や公害性、価格、油
との親和、拡散性、比重の各観点から総合的に考
慮してエタノール、イソプロパノール等を使用す
ることが好ましい。 As the alcohol, it is preferable to use ethanol, isopropanol, etc., taking comprehensive consideration from the viewpoints of toxicity, pollution, price, affinity with oil, diffusibility, and specific gravity.
通常主剤粒子の真比重は0.90〜0.98程度である
から、比重が0.78〜0.81程度の前記アルコール類
の10〜35%水溶液を作ればその比重は0.96〜0.98
となり、主剤の真比重と等しくなり、この中にお
ける主剤の分散、懸濁安定性は極めて良好とな
る。更に安定性を改良するため、極微量の界面活
性剤を添加することもできる。この場合、添加濃
度は当該界面活性剤の臨界ミセル濃度(CMC)
附近とし、海、陸水上に散布した場合稀釈効果に
より当該界面活性剤濃度がCMCを直ちに割込み、
作用が衰える如くするのが好ましい。また、当該
界面活性剤はイオン性活性剤、特に脂肪酸アルカ
リ石鹸等の陰イオン性の界面活性剤で、その金属
イオン分としてはナトリウム、カリウム、リチウ
ム等のアルカリ金属またはアンモニウムイオンが
望ましい。前記金属は、特に海水中ではカルシウ
ム、マグネシウム等のアルカリ土類金属とイオン
交換してやはり界面活性の喪失を起すものであ
る。 Normally, the true specific gravity of the main ingredient particles is about 0.90 to 0.98, so if you make a 10 to 35% aqueous solution of the alcohol with a specific gravity of about 0.78 to 0.81, the specific gravity will be 0.96 to 0.98.
This becomes equal to the true specific gravity of the base agent, and the dispersion and suspension stability of the base agent therein becomes extremely good. To further improve stability, trace amounts of surfactants can also be added. In this case, the additive concentration is the critical micelle concentration (CMC) of the surfactant.
When sprayed on sea or land water, the concentration of the surfactant immediately exceeds the CMC due to the dilution effect.
It is preferable to reduce the effect. Further, the surfactant is an ionic surfactant, particularly an anionic surfactant such as a fatty acid alkali soap, and the metal ion content thereof is preferably an alkali metal such as sodium, potassium, lithium, or ammonium ion. The metals undergo ion exchange with alkaline earth metals such as calcium and magnesium, especially in seawater, resulting in a loss of surface activity.
主剤微粒子の有機溶剤水溶液に対する懸濁濃度
は自由に調節できるが、その安定性と取扱い性、
輸送、貯蔵性等から考慮して約10〜30重量%が好
ましい。 The suspension concentration of the main agent fine particles in the organic solvent aqueous solution can be adjusted freely, but its stability and handling
It is preferably about 10 to 30% by weight in consideration of transportation, storage properties, etc.
海上等での散布にあたつては、この懸濁液状品
をポンプで吸い上げながら、またはベンチユリー
式に海水のポンプアツプで吸引し、さらに数%以
下に稀釈しながら極めて効率良く流出油面に散布
できるものである。 When spraying at sea, etc., this suspension product can be sucked up with a pump or pumped up with seawater using a ventilator method, and then diluted to less than a few percent and sprayed on the spilled oil surface extremely efficiently. It is something.
散布した後の凝集油能力は、集油量、集油速度
および凝油物硬度とも粉末での散布の場合と略同
程度に達成でき、常法による回収が可能である。 The ability to aggregate oil after spraying can be achieved in terms of oil collection amount, oil collection speed, and oil condensate hardness that are approximately the same as in the case of powder spraying, and recovery by conventional methods is possible.
以下本発明を実施例に基づいて更に具体的に説
明する。 The present invention will be explained in more detail below based on examples.
実施例 1
ポリ2−ノルボーネン(分子量200万以上、平
均粒径0.3〜0.4mm、真比重0.96)20を秤取し、
イソプロパノール(比重0.7862/20℃)28.3と
蒸溜水71.7の混合水溶液(比重0.9585/27℃)
100に装入後、室温にてホモミキサーにより
2000r・p・mで15分間撹拌し、懸濁液121を製
造した。この懸濁液15を、海水50にB重油10
を加えた二層液に散布し、約3秒間撹拌したと
ころ、約20秒後にB重油はほぼ完全にポリ2−ノ
ルボーネンに凝集され、網等で回収可能な板状固
体を形成した。Example 1 Poly 2-norbornene (molecular weight 2 million or more, average particle size 0.3 to 0.4 mm, true specific gravity 0.96) 20 was weighed out,
Mixed aqueous solution of isopropanol (specific gravity 0.7862/20℃) 28.3 and distilled water 71.7 (specific gravity 0.9585/27℃)
After charging to 100 ml, homomixer at room temperature
Suspension 121 was produced by stirring at 2000 r.p.m. for 15 minutes. Add 15 parts of this suspension to 50 parts of seawater and 10 parts of B heavy oil.
When the mixture was sprinkled onto the two-layer solution and stirred for about 3 seconds, heavy oil B was almost completely coagulated into poly-2-norbornene after about 20 seconds, forming a plate-shaped solid that could be collected using a net or the like.
なお、前記懸濁液は1週間静置しても安定で、
2週間静置後やゝ上層に分離液が見られたが、軽
度の撹拌で再び完全な懸濁液に回復した。 In addition, the suspension is stable even if left for one week,
After standing for 2 weeks, a separated liquid was observed in the upper layer, but a complete suspension was restored with slight stirring.
実施例 2
実施例1と同じポリ2−ノルボーネン20を秤
取し、エタノール(比重0.7937/15.6℃)29と
蒸溜水71の混合水溶液(比重0.960/25℃)100
に装入し、実施例1と同様の操作を行なつて懸
濁液121を製造した。この懸濁液15を、海水
50に着色灯油10を加えた油水二層液に散布
し、約3秒間撹拌したところ約15秒後に灯油はほ
ぼ完全にポリ2−ノルボーネンに凝集され網等で
回収可能な板状固体を形成した。Example 2 The same poly-2-norbornene 20 as in Example 1 was weighed out and mixed with a mixed aqueous solution (specific gravity 0.960/25°C) of ethanol (specific gravity 0.7937/15.6°C) 29 and distilled water 71 (specific gravity 0.960/25°C) 100%.
The same procedure as in Example 1 was carried out to produce suspension 121. Add 15% of this suspension to seawater
It was sprayed on a two-phase oil-water solution containing 10 parts of colored kerosene and 50 parts of colored kerosene, and stirred for about 3 seconds. After about 15 seconds, the kerosene was almost completely coagulated into poly-2-norbornene, forming a plate-shaped solid that could be collected with a net, etc. .
なお、前記懸濁液は約3日後に下層に僅少の水
分々離が認めれたが、軽度の揺動により再び完全
な懸濁状態を回復した。 Although a slight amount of water separation was observed in the lower layer of the suspension after about 3 days, a complete suspension state was restored by slight shaking.
実施例 3
アイソタクチツクポリプロピレン(分子量約40
万、比重0.90、平均粒径400〜500mμ)30を秤
取し、イソプロパノール(比重0.7862/20℃)57
と蒸溜水43との混合水溶液(比重0.90/25
℃)100に装入後、実施例1と同様の方法で懸
濁液を製造した。この懸濁液35を、海水50に
着色灯油8を加えた油水二層液に散布し、約5
秒撹拌したところ約15秒後に灯油は完全にアイソ
タクチツクポリプロピレンに凝集し、無定形の粒
径約1cmの塊状物となり、網等での回収が可能で
あつた。Example 3 Isotactic polypropylene (molecular weight approximately 40
30,000, specific gravity 0.90, average particle size 400-500 mμ) 30, and isopropanol (specific gravity 0.7862/20℃) 57
and distilled water 43 (specific gravity 0.90/25
After charging at 100 °C, a suspension was prepared in the same manner as in Example 1. This suspension (35%) was sprayed onto a two-layer oil-water solution containing 50% seawater and 8% colored kerosene.
After about 15 seconds of stirring, the kerosene completely coagulated into isotactic polypropylene and became amorphous lumps with a particle size of about 1 cm, which could be collected using a net or the like.
この懸濁液は実施例1および2のものに比較
し、やゝ静置安定性は劣つたが、軽度の撹拌で懸
濁液に回復した。 Although this suspension had slightly lower static stability than those of Examples 1 and 2, it recovered to a suspension with mild stirring.
実施例 4
実施例2に記載の方法において、脂肪酸アルカ
リ石鹸400gを添加、撹拌した。得られた懸濁液
は実施例2と同等の着色灯油に対する凝集力を示
す一方、静置安定性は半年以上であつた。Example 4 In the method described in Example 2, 400 g of fatty acid alkaline soap was added and stirred. The obtained suspension showed the same cohesive strength against colored kerosene as in Example 2, and had static stability for more than half a year.
Claims (1)
のオレフイン重合体、2−ノルボーネン重合体等
の凝油性、吸油性粉末を、比重が0.78〜0.81の低
級アルコールの10〜35%水溶液に懸濁させて成る
ことを特徴とする流出油凝集剤。 2 前記低級アルコールの水溶液中に、臨界ミセ
ル濃度に近い濃度の界面活性剤および/又はアル
カリ石鹸等の硬水耐性の小なるイオン性界面活性
剤を存在せしめて成ることを特徴とする特許請求
の範囲第1項に記載の流出油凝集剤。[Claims] 1. True specific gravity is 0.90 to 0.98 and average particle size is 1.0 to 0.5 mm.
A spilled oil flocculant characterized in that it is made by suspending an oil coagulating and oil absorbing powder such as an olefin polymer or a 2-norbornene polymer in a 10 to 35% aqueous solution of a lower alcohol having a specific gravity of 0.78 to 0.81. 2. Claims characterized in that a surfactant with a concentration close to the critical micelle concentration and/or an ionic surfactant with low resistance to hard water such as alkaline soap is present in the aqueous solution of the lower alcohol. Spilled oil flocculant according to paragraph 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15741782A JPS5947283A (en) | 1982-09-11 | 1982-09-11 | Effluent oil flocculant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15741782A JPS5947283A (en) | 1982-09-11 | 1982-09-11 | Effluent oil flocculant |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5947283A JPS5947283A (en) | 1984-03-16 |
JPH0322918B2 true JPH0322918B2 (en) | 1991-03-27 |
Family
ID=15649175
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15741782A Granted JPS5947283A (en) | 1982-09-11 | 1982-09-11 | Effluent oil flocculant |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5947283A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5982991A (en) * | 1982-11-01 | 1984-05-14 | Nippon Zeon Co Ltd | Removing or recovering method of oil |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5514109A (en) * | 1978-07-13 | 1980-01-31 | Japan Steel Works Ltd:The | Method and apparatus for drawing and forging of nozzle |
-
1982
- 1982-09-11 JP JP15741782A patent/JPS5947283A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5514109A (en) * | 1978-07-13 | 1980-01-31 | Japan Steel Works Ltd:The | Method and apparatus for drawing and forging of nozzle |
Also Published As
Publication number | Publication date |
---|---|
JPS5947283A (en) | 1984-03-16 |
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