WO1998046530A1 - Procede d'extraction du petrole - Google Patents
Procede d'extraction du petrole Download PDFInfo
- Publication number
- WO1998046530A1 WO1998046530A1 PCT/JP1998/001734 JP9801734W WO9846530A1 WO 1998046530 A1 WO1998046530 A1 WO 1998046530A1 JP 9801734 W JP9801734 W JP 9801734W WO 9846530 A1 WO9846530 A1 WO 9846530A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- oil
- latex
- coagulant
- emulsion
- seawater
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K3/00—Materials not provided for elsewhere
- C09K3/32—Materials not provided for elsewhere for absorbing liquids to remove pollution, e.g. oil, gasoline, fat
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0202—Separation of non-miscible liquids by ab- or adsorption
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S210/00—Liquid purification or separation
- Y10S210/918—Miscellaneous specific techniques
- Y10S210/922—Oil spill cleanup, e.g. bacterial
- Y10S210/925—Oil spill cleanup, e.g. bacterial using chemical agent
Definitions
- the present invention relates to a method for recovering oil, for example, recovering heavy oil and crude oil spilled to the sea due to a tanker accident or the like, recovering oil adhering to a reef or a shore, recovering oil leaking from an oil tank or the like, Background technology for collecting and removing oil adhering to washing tanks, etc.
- Heavy oil and crude oil may spill into seawater due to tanker accidents. Heavy oil and crude oil are mixtures of aromatic oils (aloma oils), naphthenic oils, paraffin oils, etc., and contain large amounts of aromatic oils.
- the spilled heavy oil or crude oil has a lower specific gravity than seawater, so it initially forms a lump and floats on the sea surface.
- Baraffin oil and naphthenic oil which have low viscosity, are gradually dispersed and separated from the oil lump by waves and tidal currents. A dense aromatic oil will remain and sink into the sea. Some of the oil spilled in this way adheres to the shore, and the adhered oil sticks to rocks, etc., and is difficult to remove.
- Known methods for treating spilled oil include methods that rely on humans, such as collecting and pumping oil with an oil fence, etc., as well as methods such as decomposing with crude oil decomposing bacteria and mixing oil into seawater with an emulsifier.
- the dispersants used for this purpose, emulsifiers and crude oil degrading bacteria make the oil finer, emulsify and disperse it into a state that is easy to mix with seawater, and have a natural purification action (microbial decomposition by bacteria, transpiration by solar radiation) Oxidizing action, etc.), but the action is slow, and in the case of a large number of oil spills, the dispersant
- the oil is also diffused and diluted in uncontaminated areas, making oil recovery more difficult and impractical. Therefore, in practice, oil that has been spilled manually is collected.
- an object of the present invention is to provide a method for easily recovering, for example, spilled oil. It is another object of the present invention to provide a method for collecting oil while minimizing environmental pollution, and to provide a method for easily collecting and removing oil attached to a solid surface. Disclosure of the invention
- the latex and its coagulant are separately sprayed on water containing oil, whereby the latex is diffused around the oil in the water, coagulated by the coagulant, and It is characterized by forming and collecting a solidified latex film around the oil.
- the latex may be a synthetic rubber latex or a hydrophilic polymer emulsion such as polyvinyl acetate or polyvinyl alcohol in addition to the natural rubber latex.
- the latex is a hydrophilic colloid solution.
- the dispersion medium is water, and the dispersoid is a polymer compound.
- a polymer emulsion prepared by emulsion polymerization is suitable because it is an emulsion from the beginning, but is not limited to this.
- the most preferred latex is natural rubber latex, which is a cis 1,4-isoprene polymer (approximately 54% by weight, the following concentration is expressed in units of% by weight), water (approximately 44%) and protein (2%). Degree).
- Any coagulant can be used as long as it coagulates the latex.
- polyvalent metal ions, polyvalent nonmetal ions, organic acids, and alkalis such as ammonia are used.
- the most preferred are salts of Mg and Ca, especially Mg and Ca chloride.Since these are originally contained in the environment such as seawater, there is no danger of secondary pollution. It is inexpensive.
- the present invention also relates to a method in which a lipophilic polymer emulsion is brought into contact with oil on a solid surface such as a rock or a tank wall, solubilizes the oil in the emulsion, and then solidifies the emulsion to form an oil. It is characterized by being collected.
- a lipophilic polymer emulsion is an emulsion in which water is dispersed as a discontinuous phase in an oily continuous phase. And parents Use a highly oily emulsion.
- Latex When latex is sprayed around the oil, etc., which has spilled into the sea, using a hose, etc., the latex diffuses into the water because it is a hydrophilic mouth. The sprayed latex reacts with the coagulant and coagulates. Since the specific gravity of the solid after coagulation is smaller than that of water, the latex floats and forms a film around the oil. Latex that has entered the oil mass of the spilled oil does not coagulate as it is, but water generally enters the oil mass, and the latex solidifies upon contact with the oil-water interface due to waves.
- the coagulated latex film does not dissolve in the oil, but has good affinity with the oil, collects at the interface between the spilled oil and water, adheres to the interface of the spilled oil, and coagulates the latex film (hereinafter simply referred to as The latex membrane) has a low viscosity so that oil spills can be easily recovered, the latex membrane is lighter than water, preventing aroma oil from settling, and the spilled oil is surrounded by a latex membrane to form oil lumps. Prevent dispersion.
- the oil mass surrounded by the latex film is not sticky and does not adhere to rocks or sand even if it drifts on the shore. Furthermore, the coagulation rate of latex is less dependent on water temperature, and oil spills can be recovered even in winter or cold regions.
- this invention is mainly used to recover oil spills in seawater.
- Coagulants such as Mg chloride and Ca chloride exist in seawater, but latex coagulation is slow at natural concentration and sprayed. Spraying of coagulant is necessary because latetus is unnecessarily diffused and inefficient.
- the coagulant is sprayed separately from the latex with a separate hose, etc., but the latex and the coagulant may be mixed in the spray nozzle, and the mixture may be sprayed with the spray pressure (in this case, the nozzle).
- the concentration of the coagulant is adjusted to delay the action of the coagulant, or the residence time in the nozzle after mixing is reduced to the time required for coagulation. What is necessary is just to make it short enough.
- Mg or Ca salts such as Mg chloride and Ca chloride are used as the coagulant, they do not pollute the environment because they are naturally occurring salts in seawater.
- the latex may be a mixture of multiple latexes.
- a decomposing enzyme particularly an enzymatic decomposing enzyme in latex, can be added to decompose unrecovered latex and prevent secondary contamination.
- a lipophilic polymer emulsion for the oil attached to rocks.
- This is a substance in which the lipophilic substance is a continuous phase and water is a discontinuous phase.
- the adhering oil is taken into the emulsion, and when the emulsion is coagulated with a coagulant, it gels and the oil is recovered from rocks and the like. Can be excluded.
- the present invention is not limited to the recovery of crude oil and heavy oil in seawater, but can be used for any purpose as long as it recovers oil spilled into water.
- the present invention can be used not only for collecting and removing oil adhering to rocks, but also for removing oil adhering to, for example, a wall surface of a tank.
- Contaminated stones collected on the coast of Mikuni contaminated by a stone weighing about 10 kg
- the oil is fully adhered), immersed in natural latex, one of the polymer emulsions, pulled up for 2 seconds, and rubbing the stone surface strongly with a cloth, causing a large amount of fine lumps of polymer particles.
- the adhesive layer of the contaminated oil became fine aggregates contained in the latex and could be easily removed.
- the oil in the fine depressions could be easily removed using a brush. This was an application of the destabilization (agglomeration phenomenon) action that promoted the destruction of the stable state from the stable state of the latex due to the dynamic shear force without using a coagulant.
- bitter powder main component is Mg chloride
- the water temperature was about 10 ° C, but when the water temperature was 0 ° C, the time until the seawater became transparent again was about 230 seconds, and when it was 30 ° C, it was 200 seconds. Thus, the water temperature dependence of the time until a latex film was formed around C heavy oil was small.
- the heavy fuel oil wrapped in the latex membrane is easy to recover because it has no tackiness, and the fluidity is low because 100 g of heavy fuel oil is formed into a single ball, and the latex film on the surface is white rubber-like.
- the overall color was white-gray-gray-black, mottled because the color of Fuel Oil C inside was visible.
- the latex had a solids content of 70% and was stabilized at a pH of about 11.
- a latex film was formed around the oil and formed into a ball.
- the seawater became transparent again.
- the time until the seawater becomes transparent due to the formation of a latex film is called the solidification time.
- the latex had a solids content of 65%.
- As a coagulant 20 g of a solution of 60 g of calcium nitrate dissolved in 100 cc of methanol was used. A latex film was formed around the oil and formed into a ball, and in 33 seconds, the seawater became transparent again.
- Comparative Example 1 The test was performed under the same conditions as in Experimental Example 1 (water temperature: 10 ° C) except that no coagulant was used. In this case, the emulsion dispersed in the seawater remained milky, and the seawater did not become transparent for a long time, and it took five days for it to become completely transparent. Practically, emulsions that do not solidify due to waves and tidal currents are diffused into seawater, with no favorable results.
- Fuel oil C was sprinkled on the surface of the rock to form an oil slick, which was allowed to stand outdoors for 2 days (at an air temperature of 0 ° (: ⁇ 10 ° C). After that, 100 weight of natural rubber latex was used as lipophilic emulsion. Parts by weight, 2 parts by weight of nonylphenol ether and 2 parts by weight of polyoxyethylene alkyl ether, 1.5 parts by weight of colloidal sulfur, 1.5 parts by weight of ⁇ No. 1 with stirring, and spinning A mixed emulsion containing 15 parts by weight of dollar oil was used, and this emulsion was applied to the surface of the oil film with a brush.
- a silicate-based compound such as Na 2 S i F 6 as a coagulant
- the coagulant will be coagulated due to its heat sensitivity. Is promoted and can be solidified more quickly.
- the latex and its coagulant are dispersed in oil-containing water to diffuse the latex around the oil in the water and coagulate with the coagulant.
- a method for collecting oil characterized by forming and collecting a solidified latex film around oil in water.
- the oil recovery method may be characterized in that the latex is natural rubber latex, and the coagulant is a Mg or Ca salt and the oil is heavy oil in seawater. Alternatively, it may be characterized by being crude oil.
- the lipophilic polymer emulsion is brought into contact with the oil on the solid surface to solubilize the oil in the emulsion, and then the oil is recovered by solidifying the emulsion.
- the oil recovery method may be characterized by the following.
- the coagulant has the following effects.
- Polymer particles such as latex are dispersed uniformly in water as emulsion in a colloidal state, and destabilize those that are in a stable state.
- a substance is called a coagulant.
- the coagulant is an anxiety agent, and may also be called a gelling agent or a flocculant.
- coagulation is a phenomenon in which the polymer in the latex or the like is separated from the serum as agglomerates. At this time, the serum loses the polymer and becomes transparent, or even if it is not completely lost. Concentration decreases. In this way, the solidified polymer is referred to as coagulum or coagulum (coagulum).
- Gelation is a phenomenon in which the latex in a solution loses fluidity and the whole solidifies into a gelatinous shape while maintaining the shape of the container.The product is called a gel. Separate the clear serum. This phenomenon is referred to as syneresis (syne res iss).
- Aggregation refers to the phenomenon that a large amount of fine agglomerates (agg1omerates) of polymer particles are generated.
- coagulants chemicals that promote the destruction of the stable state of normal emulsions, such as latetus, are referred to as coagulants or destabilizers.
- the concept of emulsion-latex in the present invention will be described.
- polymer emulsion latex There are a large number of varieties of polymer emulsion latex, and various methods are used to classify them. The major categories are classified as shown in Table 1 based on the manufacturing method or production process.
- the dispersoid is generally referred to as a polymer (polymethyl) and the dispersion medium is water or other liquid.
- a stable state in which the polymer (polymethyl) becomes a discontinuous phase and water or other liquid is a continuous phase.
- the oil recovery method of the present invention for example, the recovery of heavy oil or crude oil that has flown offshore due to a tanker accident, the recovery of oil attached to a reef or coast, or the oil tank It is possible to easily collect the oil leaked from the tank, and to collect and remove the oil adhering to the tank when washing the tank.
- Classification of emulsion and latex by polymer for example, the recovery of heavy oil or crude oil that has flown offshore due to a tanker accident, the recovery of oil attached to a reef or coast, or the oil tank It is possible to easily collect the oil leaked from the tank, and to collect and remove the oil adhering to the tank when washing the tank.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Public Health (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Removal Of Floating Material (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Cleaning Or Clearing Of The Surface Of Open Water (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Liquid Carbonaceous Fuels (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002286834A CA2286834C (en) | 1997-04-16 | 1998-04-16 | Process for recovering oils |
US09/403,088 US6264398B1 (en) | 1997-04-16 | 1998-04-16 | Process for the recovery of oil |
AU68520/98A AU6852098A (en) | 1997-04-16 | 1998-04-16 | Process for recovering oils |
DE69830722T DE69830722T2 (de) | 1997-04-16 | 1998-04-16 | Verfahren zur rückgewinnung von ölen |
EP98914040A EP0979802B1 (en) | 1997-04-16 | 1998-04-16 | Process for recovering oils |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9115217A JPH10292358A (ja) | 1997-04-16 | 1997-04-16 | 油分の回収方法 |
JP9/115217 | 1997-04-16 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1998046530A1 true WO1998046530A1 (fr) | 1998-10-22 |
Family
ID=14657271
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP1998/001734 WO1998046530A1 (fr) | 1997-04-16 | 1998-04-16 | Procede d'extraction du petrole |
Country Status (9)
Country | Link |
---|---|
US (1) | US6264398B1 (ja) |
EP (1) | EP0979802B1 (ja) |
JP (1) | JPH10292358A (ja) |
CN (1) | CN1108278C (ja) |
AU (1) | AU6852098A (ja) |
CA (1) | CA2286834C (ja) |
DE (1) | DE69830722T2 (ja) |
RU (1) | RU2179156C2 (ja) |
WO (1) | WO1998046530A1 (ja) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001000774A (ja) * | 1999-06-21 | 2001-01-09 | Hinomaru Carbo Techno Kk | 洗濯機用浄化装置 |
AUPS161202A0 (en) * | 2002-04-08 | 2002-05-16 | Robinson, David Charles | Oil recovery and environmental cleanup system |
NO331717B1 (no) * | 2009-10-12 | 2012-03-05 | Ingmar Johan Hogoy | Fremgangsmate for isolering av en forurensing som flyter pa overflaten av sjoen med en polymerisert polymerblanding. |
EP2593406A1 (en) * | 2010-07-14 | 2013-05-22 | Ellingsen, Hans Falnes | Natural -origin enzymatic bioremediation with wide applicability, the substrate being an environment consisting of extracts from oleaginous vegetable sources added to an isomer mixture |
EP2439341A1 (en) * | 2010-10-07 | 2012-04-11 | Vetco Gray Controls Limited | Removing oil from the surface of a body of water |
KR101397652B1 (ko) * | 2012-07-10 | 2014-05-22 | 주식회사 워켐 | 유흡착용 유류고형화제 조성물 및 그 제조방법 |
AU2021106778B4 (en) * | 2020-09-25 | 2022-09-08 | Sustainable Rubber Technologies (SRT) Pty Ltd | An in situ decontamination method and apparatus |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5041354A (ja) * | 1973-08-14 | 1975-04-15 | ||
JPS5168968A (en) * | 1974-12-11 | 1976-06-15 | Nippon Paint Co Ltd | Osenbutsushitsuno jokyoho |
JPH05309369A (ja) * | 1992-04-30 | 1993-11-22 | Showa Shell Sekiyu Kk | 油処理剤 |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3198731A (en) * | 1961-09-20 | 1965-08-03 | Yosemite Chemical Co | Method of treating oil on the surface of water |
GB992524A (en) * | 1962-12-31 | 1965-05-19 | Internat Synthetic Rubber Comp | Method for cleaning up and removal of oil pollution on the surface of water |
DE1484374B2 (de) * | 1964-01-30 | 1973-05-24 | Seger, Paul, 2000 Hamburg | Verfahren zur beseitigung von auf oberflaechen, insbesondere wasseroberflaechen, befindlichen oelschichten |
US3457168A (en) * | 1968-03-08 | 1969-07-22 | Sun Oil Co | Procedure for disposing of petroleum oil on a water surface |
US3919083A (en) * | 1970-07-24 | 1975-11-11 | Loctite Ireland Ltd | Treatment of floating pollutants |
JPS5015006B1 (ja) * | 1970-11-07 | 1975-06-02 | ||
US3977969A (en) * | 1971-10-26 | 1976-08-31 | The United States Of America As Represented By The Secretary Of The Navy | Containment and riddance of oil spills |
DE2208748A1 (de) * | 1972-02-24 | 1973-08-30 | Dura Tufting Gmbh | Verfahren und vorrichtung zum reinigen von mit oel verunreinigtem wasser |
JPS603116B2 (ja) * | 1977-02-17 | 1985-01-25 | 三菱レイヨン株式会社 | 含油廃水処理剤の製造方法 |
JPS53113283A (en) * | 1977-03-14 | 1978-10-03 | Agency Of Ind Science & Technol | Method of producing coagulant for spilled oil |
DE3070952D1 (en) * | 1979-06-26 | 1985-09-12 | British Petroleum Co Plc | Cross-linked polymer compositions and production thereof |
CN85109534B (zh) * | 1985-12-31 | 1988-03-09 | 云南师范大学 | 盐卤石灰沉淀除铅法 |
CA2094044A1 (en) * | 1990-11-02 | 1992-05-14 | Guy Imre Zoltan Kalocsai | Reversible transformation of hydrocarbons |
CA2036396C (en) * | 1991-02-15 | 2006-05-02 | William Ernest Nelson | Process to solidify oil on land and sea |
DE4115749A1 (de) * | 1991-05-15 | 1992-11-19 | Franz Xaver Appel | Verfahren zur beseitigung von oelen und/oder oelhaltigen emulsionen |
US5262059A (en) * | 1992-12-15 | 1993-11-16 | Cal-Sine Environmental, Inc. | Method of removing organic contaminants from water |
US5437793A (en) * | 1993-06-08 | 1995-08-01 | Mansfield & Alper, Inc. | Coagulant for oil glyceride/isobutyl methacrylate composition and method of use |
-
1997
- 1997-04-16 JP JP9115217A patent/JPH10292358A/ja active Pending
-
1998
- 1998-04-16 WO PCT/JP1998/001734 patent/WO1998046530A1/ja active IP Right Grant
- 1998-04-16 CA CA002286834A patent/CA2286834C/en not_active Expired - Fee Related
- 1998-04-16 EP EP98914040A patent/EP0979802B1/en not_active Expired - Lifetime
- 1998-04-16 DE DE69830722T patent/DE69830722T2/de not_active Expired - Fee Related
- 1998-04-16 RU RU99121856/12A patent/RU2179156C2/ru not_active IP Right Cessation
- 1998-04-16 CN CN98804210A patent/CN1108278C/zh not_active Expired - Fee Related
- 1998-04-16 US US09/403,088 patent/US6264398B1/en not_active Expired - Fee Related
- 1998-04-16 AU AU68520/98A patent/AU6852098A/en not_active Abandoned
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5041354A (ja) * | 1973-08-14 | 1975-04-15 | ||
JPS5168968A (en) * | 1974-12-11 | 1976-06-15 | Nippon Paint Co Ltd | Osenbutsushitsuno jokyoho |
JPH05309369A (ja) * | 1992-04-30 | 1993-11-22 | Showa Shell Sekiyu Kk | 油処理剤 |
Also Published As
Publication number | Publication date |
---|---|
CN1108278C (zh) | 2003-05-14 |
AU6852098A (en) | 1998-11-11 |
DE69830722T2 (de) | 2006-04-20 |
CA2286834A1 (en) | 1998-10-22 |
CN1252776A (zh) | 2000-05-10 |
DE69830722D1 (de) | 2005-08-04 |
RU2179156C2 (ru) | 2002-02-10 |
JPH10292358A (ja) | 1998-11-04 |
EP0979802A4 (en) | 2001-01-24 |
EP0979802A1 (en) | 2000-02-16 |
EP0979802B1 (en) | 2005-06-29 |
US6264398B1 (en) | 2001-07-24 |
CA2286834C (en) | 2005-03-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN1458076A (zh) | 废弃钻井液混凝脱水处理方法 | |
US20170320759A1 (en) | Oil sands tailings treatment | |
US5104548A (en) | Controlling and recovering oil spills from the environment | |
US4941978A (en) | Controlling and recovering oil spills from the environment | |
KR20180004157A (ko) | 토양 또는 경질 표면 세정용 제품 및 그 적용 방법 | |
WO1998046530A1 (fr) | Procede d'extraction du petrole | |
JP2001089574A (ja) | ポリビニルアルコール系含水ゲル、その製造方法及び排水処理装置 | |
RU2007137062A (ru) | Способ получения гранул из политетрафторэтилена, содержащих наполнитель | |
US5490940A (en) | Method for forming mineral solids-oil floccules | |
CA1169737A (en) | Method of treating water-in-oil dispersions | |
US3265616A (en) | Method of cleaning or collecting oil from the surface of an area of water | |
US3503774A (en) | Method of cleaning oil-contaminated particulate materials | |
US3732162A (en) | Method of removing oil spills from water | |
CA1107267A (en) | Absorbent composition for oil and the like | |
US5118425A (en) | Method for removing oil or hydrocarbons from water | |
US5259973A (en) | Treatment of spills with gelatin | |
JPS5870807A (ja) | ポリアクリルアマイド系固形凝集剤の製法 | |
JPH10273650A (ja) | 被処理油の処理方法及び固形燃料 | |
KR101663577B1 (ko) | 폐생물자원 유래 젤라틴 수용액을 포함하는 해상 유출유 처리용 겔화제 | |
KR100298655B1 (ko) | 유류 고형화제 | |
JP2524111B2 (ja) | 流体の汚濁物質分離剤 | |
RU2148024C1 (ru) | Средство для очистки поверхности воды от нефти и нефтепродуктов | |
RU2145333C1 (ru) | Средство для очистки воды от нефти и нефтепродуктов | |
KR20200090745A (ko) | 유체로부터 불순물을 제거하기 위한 조성물 및 방법 | |
EP2488456B1 (en) | Organic oil boom |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WWE | Wipo information: entry into national phase |
Ref document number: 98804210.X Country of ref document: CN |
|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AL AM AT AU AZ BA BB BG BR BY CA CH CN CU CZ DE DK EE ES FI GB GE HU IL IS KE KG KR KZ LC LK LR LS LT LU LV MD MG MK MN MW MX NO NZ PL PT RO RU SD SE SG SI SK TJ TM TR TT UA UG US UZ VN |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
ENP | Entry into the national phase |
Ref document number: 2286834 Country of ref document: CA Ref document number: 2286834 Country of ref document: CA Kind code of ref document: A |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1998914040 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 09403088 Country of ref document: US |
|
REG | Reference to national code |
Ref country code: DE Ref legal event code: 8642 |
|
WWP | Wipo information: published in national office |
Ref document number: 1998914040 Country of ref document: EP |
|
WWG | Wipo information: grant in national office |
Ref document number: 1998914040 Country of ref document: EP |