WO1998012239A1 - Polymeric material - Google Patents
Polymeric material Download PDFInfo
- Publication number
- WO1998012239A1 WO1998012239A1 PCT/GB1997/002529 GB9702529W WO9812239A1 WO 1998012239 A1 WO1998012239 A1 WO 1998012239A1 GB 9702529 W GB9702529 W GB 9702529W WO 9812239 A1 WO9812239 A1 WO 9812239A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- compound
- groups
- solvent
- polymeric compound
- polymeric
- 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.)
- Ceased
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F246/00—Copolymers in which the nature of only the monomers in minority is defined
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2/00—Processes of polymerisation
- C08F2/04—Polymerisation in solution
- C08F2/06—Organic solvent
Definitions
- This invention relates to a polymeric material and particularly, although not exclusively, relates to a polymeric material which is at least partially formed from a 1 , 2-substituted ethene compound, for example a substituted styrylpyridinium compound.
- UK Patent No. GB 2 030 575 B (Agency of Science and Technology) describes a photosensitive resin which is prepared by reacting a styryl pyridinium salt which possesses a formyl or acetal group on the styryl phenyl group with a polyvinyl alcohol or a partially saponified polyvinyl acetate.
- the present invention is based on the discovery of surprising properties of 1, 2-substituted ethene compounds of the type described which allow polymeric materials to be prepared which have various useful properties.
- a method of preparing a first polymeric compound which comprises providing a compound of general formula
- R 1 and R 2 are independently selected from a hydrogen atom or an optionally substituted, preferably unsubstituted, alkyl group.
- R 1 and R 2 represent the same atom or group.
- R 1 and R 2 represent a hydrogen atom.
- said solvent is a polar solvent.
- said solvent is an aqueous solvent. More preferably, said solvent consists essentially of water.
- said compound of general formula I is provided in said solvent at a concentration at which molecules of said compound aggregate. Aggregation of said compound of general formula I may be shown or inferred from the results of various analyses as hereinafter described and any one or more of such analyses may be used. Preferably, said compound of general formula I is provided in said solvent at or above a concentration suggested by relevant vapour pressure measurements as being a point of aggregation of the compound.
- the molecules align with groups A and B adjacent to one another.
- Said compound of general formula I may be provided in said solvent at a concentration of at least 0.5 wt%, preferably at least 1.0 wt% and, more preferably, at least 1.5 wt%.
- the method comprises inducing a photochemical reaction, suitably using ultraviolet light.
- light of up to 500 nm wavelength is used.
- a and B are independently selected from optionally-substituted alkyl, cycloalkyl, cycloalkenyl, cycloalkynyl, aromatic and heteroaromatic groups. Where group A or B has a cyclic structure, five or, more preferably, six membered rings are preferred.
- a and B are independently selected from optionally substituted aromatic and heteroaromatic groups, with five or, more preferably, six-membered such groups being especially preferred.
- Preferred heteroato s of said heteroaromatic groups include nitrogen, oxygen and sulphur atoms of which oxygen and especially nitrogen, are preferred.
- Preferred heteroaromatic groups include only one heteroatom.
- optionally substituted groups described herein may be substituted by halogen atoms, and optionally substituted alkyl, acyl, acetal, hemiacetal, acetalalkyloxy, hemiacetalalkyloxy, nitro, cyano, alkoxy, hydroxy, amino, alkylamino, sulphinyl, alkylsulphinyl, sulphonyl, alkylsulphonyl, sulphonate, amido, alkylamido, alkylcarbonyl, alkoxycarbonyl, halocarbonyl and hal ⁇ alkyl groups.
- up to 3 more preferably up to 1 optional substituents may be provided on an optionally substituted group.
- an alkyl group may have up to 10, preferably up to 6, more preferably up to 4 carbon atoms, with methyl and ethyl groups being especially preferred.
- a and B each represent polar atoms or groups.
- a and B represent different atoms or groups.
- one of groups A and B includes an optional substituent which includes a carbonyl or acetal group with a for yl group being especially preferred.
- the other one of groups A and B may include an optional substituent which is an alkyl group, with an optionally substituted, preferably unsubstituted, C M alkyl group, for example a methyl group, being especially preferred.
- x is an integer from 1 to 6 and each R 3 is independently an alkyl or phenyl group or together form an alkalene group.
- group B represents a group of general formula
- R 4 represents a hydrogen atom or an alkyl or aralkyl group
- R 5 represents a hydrogen atom or an alkyl group
- X " represents a strongly acidic ion.
- Preferred compounds of general formula I for use according to the present invention include those referred to on page 3 line 8 to line 39 of GB 2 030 575 B and said compounds are hereby incorporated into this specification.
- Compounds of general formula I for use according to the present invention may be prepared as described in GB 2 030 575 B and such preparatory methods are also hereby incorporated into this specification.
- the invention extends to a novel first polymeric compound preparable by a method according to said first aspect.
- a method of preparing a formulation comprising providing a first polymeric compound according to said first or second aspects in a solvent together with a second polymeric compound and intimately mixing the compounds .
- said second polymeric compound includes one or more functional groups capable of reacting with said first polymeric compound, preferably in an acid catalysed reaction. Said reaction is preferably a condensation reaction.
- said second polymeric compound includes a functional group selected from an alcohol, carboxylic acid, carboxylic acid derivative, for example an ester, and an amine group.
- Preferred second polymeric compounds include optionally substituted, preferably unsubs t i tu t ed , p o 1 y v i ny 1 a 1 c oho 1 , polyvinylacetate, polyalkylene glycols, for example polypropylene glycol, and collagen (and any component thereof) .
- said second polymeric compound is a solid under ambient conditions.
- said intimate mixing is carried out at an elevated temperature.
- mixing is carried out in the same solvent in which compound I is prepared.
- the mixture may include further polymeric compounds which may be the same type as said second polymeric compounds described above.
- the ratio of the wt% of said first polymeric compound to the wt% of said second polymeric compound (or the sum of the wt% of the second compound and any further compounds) in the mixture is found to influence significantly the properties of the formulation prepared.
- the ratio of the wt% of said first polymeric compound to that of said second polymeric compound may be in the range 0.01 to 100, is preferably in the range 0.05 to 50 and more preferably in the range 0.3 to 20.
- water is removed from said formulation to produce a solid material, for example in the form of a film.
- a formulation comprising a first polymeric compound according to said first or second aspects and a second polymeric compound as described in said third aspect.
- said formulation is provided in a solid form.
- a method of preparing a material for example a colloid or a gel comprising providing a mixture prepared in said third aspect or a mixture according to said fourth aspect in a solvent and causing the first and second polymeric compounds to react with one another.
- the reaction may be acid catalysed and, accordingly, the method may include the step of providing an acid in the mixture. It is found that the concentration of acid used affects the rate of colloid/gel production. Preferably, at least 0.05 wt%, more preferably at least 0.1% of an acid is used. Any acid may be used whether organic or inorganic. Preferred acids include paratoluene sulphonic acid, hydrochloric acid, phosphoric acid, sulphonic acid and napthalene sulphuric acids.
- the concentration of the mixture used affects whether a colloid or gel forms. Where the wt% of a said solid formulation of said first and second polymeric compound is less than about 2 wt%, a visco-elastic colloidal solution is formed. On the other hand, where the concentration is greater than about 2 wt%, a gel may be formed.
- a further active ingredient may be incorporated into the colloid or gel prepared as described in said fifth aspect, suitably by addition of said active ingredient prior to the reaction of the first and second polymeric compounds.
- Preferred active ingredients include antibacterial agents, for example an iodine/iodide mixture, cetyl trimethyl ammonium bromide and neomycin sulphate.
- Sheet materials may be prepared incorporating active ingredients and since it is understood that preparations prepared as described herein are biocompatible, the sheet materials may be used in burns treatment.
- the invention provides a method of collecting and/or isolating and/or emulsifying oil (or the like) which comprises contacting oil (or the like) with a reaction mixture according to said fifth aspect so that said oil (or the like) becomes incorporated into a material, for example a gel which is formed.
- the invention extends to a colloid or gel preparable by the method of the fifth aspect.
- a novel third polymeric material which comprises the reaction product of a compound of general formula IV with a second polymeric material as described herein.
- Figure 1 is a graph showing vapour pressure measurements on aqueous solutions of 4- (4- formylphenylethenyl) -1-methylpyridinium methosulphonate (SbQ) at 37°C as a function of concentration;
- Figure 2 is a representation of the predicted energy minimised structure of four SbQ molecules in water;
- Figure 3 is a graph showing surface tension measurements of SbQ solutions, at 25°C, as a function of concen ration
- Figure 4 is a graph showing molar conductance values of SbQ solutions, at 25°C, as a function of concentration
- Figure 5 is a graph showing apparent molar volume values of SbQ, at 25°C, as a function of concentration
- Figure 6 is a graph showing Rayleigh scattering at 90° of SbQ solutions, at 25°C, as a function of concentration
- Figure 7 is a graph showing heats of dilution of SbQ solutions, at 25°C, as a function of concentration.
- the ratio ⁇ t/C represents the difference in temperature between the solvent reference probe and the solution probe at a concentration C in g/kg.
- the plot shows two linear regions, both with good correlation coefficients of 0.996 and 0.998 respectively, intersecting at a concentration value of 1.25% w/w.
- the intercept of the low range of solution concentrations was utilised in the usual manner to -yield a value for the number average molar mass for SbQ of 341, close to the expected value of 335.
- the difference of slope at the higher concentrations suggests that, above the concentration of 1.25% w/w, some form of aggregation of SbQ molecules has occurred.
- the molar conductance values of Figure 4 also show the pattern expected of a icellar forming species, with the change of slope at the cmc occurring at 0.04M.
- the sharp change of slope seen at 0.04M means that the SbQ molecule adopts a more compact form above this concentration, exactly what might be expected to happen when aggregating to form a micelle.
- the heats of dilution measurements also show a sharp change of slope, in this case at 0.035M, yet again indicating a major change in the solution state of the solute, from monomer to micelle has occurred.
- Example 2 The film described in Example 2 may be re-dissolved in water together with an acid, for example paratoluene sulphuric acid. This causes an acid catalysed aldol condensation reaction according to the scheme below.
- an acid for example paratoluene sulphuric acid. This causes an acid catalysed aldol condensation reaction according to the scheme below.
- the concentration of film used affects the properties of the resultant gel. For example, rigid gels are formed at concentrations greater than 2.5 wt%.
- the gelling time is dependent on the concentration of acid used. 0.1 wt% acid gives a gelling time of 16 hours, whereas 1 wt% acid gives a gelling time of 10 minutes.
- the gels are rigid and optically clear.
- the time required for gelation can be controlled by varying the concentration of acid used to catalyse the gelling reaction.
- the variable gel time permits the casting of different shapes of gel merely by pouring the reaction mixture into a mould. There is no significant shrinkage of the material on gel formation.
- the gels are insoluble in all common organic solvents, although some gels swell slightly. The gels are also insoluble in aqueous solutions.
- Rigid gels can be produced using a mixture of 50 wt% collagen and 50 wt% poly(vinyl alcohol) instead of only poly(vinyl alcohol) described in Examples 2 and 3.
- the gels produced show resistance to organic solvents and limited swelling in water.
- Example 6 After addition of the acid to catalyse the gelling reaction in Example 3, up to 50 wt% oil may be emulsified by the reaction mixture. The resultant gel which is formed holds the oil in a solid matrix.
- Gels can be produced using solvent mixtures containing up to 50 wt% polypropylene glycol 400.
- the swelling behaviour of the resultant gels in water is controlled by the amount of polypropylene glycol in the solvent.
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
- Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)
- Polymerisation Methods In General (AREA)
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
Abstract
Description
Claims
Priority Applications (8)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51439898A JP4159609B2 (en) | 1996-09-18 | 1997-09-16 | Polymer material |
| EP97919164A EP0935622A1 (en) | 1996-09-18 | 1997-09-16 | Polymeric material |
| CA002266578A CA2266578C (en) | 1996-09-18 | 1997-09-16 | Polymeric material |
| AU43097/97A AU734288C (en) | 1996-09-18 | 1997-09-16 | Polymeric material |
| NZ335075A NZ335075A (en) | 1996-09-18 | 1997-09-16 | Polymeric material partially formed from a 1, 2-substituted ethene compound |
| BR9712059-6A BR9712059A (en) | 1996-09-18 | 1997-09-16 | Polymeric material. |
| NO19991276A NO991276L (en) | 1996-09-18 | 1999-03-16 | Polymeric material |
| US10/644,879 US20040072946A1 (en) | 1996-09-18 | 2003-08-21 | Polymeric material |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB9619419.6 | 1996-09-18 | ||
| GBGB9619419.6A GB9619419D0 (en) | 1996-09-18 | 1996-09-18 | Polymeric material |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US26909599A Continuation | 1996-09-18 | 1999-06-07 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1998012239A1 true WO1998012239A1 (en) | 1998-03-26 |
Family
ID=10800073
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/GB1997/002529 Ceased WO1998012239A1 (en) | 1996-09-18 | 1997-09-16 | Polymeric material |
Country Status (11)
| Country | Link |
|---|---|
| EP (1) | EP0935622A1 (en) |
| JP (2) | JP4159609B2 (en) |
| CN (1) | CN1217967C (en) |
| AU (1) | AU734288C (en) |
| BR (1) | BR9712059A (en) |
| CA (1) | CA2266578C (en) |
| GB (2) | GB9619419D0 (en) |
| NO (1) | NO991276L (en) |
| NZ (1) | NZ335075A (en) |
| RU (1) | RU2249603C2 (en) |
| WO (1) | WO1998012239A1 (en) |
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003083259A2 (en) | 2002-03-28 | 2003-10-09 | Advanced Gel Technology Limited | Recovering materials |
| WO2003102052A1 (en) * | 2002-05-31 | 2003-12-11 | Advanced Gel Technology Limited | Dispersion |
| WO2004083589A2 (en) | 2003-03-20 | 2004-09-30 | Agt Energy Limited | Restricting fluid passage and novel materials therefor |
| WO2005033469A1 (en) * | 2003-10-02 | 2005-04-14 | Agt Energy Limited | Cleaning contaminated materials |
| WO2005040669A1 (en) * | 2003-10-02 | 2005-05-06 | Proflux Systems Llp | Method for reducing the viscosity of viscous fluids |
| WO2005040553A1 (en) * | 2003-10-02 | 2005-05-06 | Agt Energy Limited | Fracturing of subterranean formations |
| GB2428241A (en) * | 2002-11-05 | 2007-01-24 | Univ Bradford | Polymeric material |
| US7281579B2 (en) * | 2001-12-07 | 2007-10-16 | Aqueolic Canada Ltd. | Method for terminating or reducing water flow in a subterranean formation |
| WO2008152357A1 (en) | 2007-06-15 | 2008-12-18 | Proflux Systems Llp | Hydrocarbons |
| EP2018191A2 (en) * | 2006-05-17 | 2009-01-28 | AGT Sciences Limited | Delivery means |
| US7832478B2 (en) | 2007-11-07 | 2010-11-16 | Schlumberger Technology Corporation | Methods for manipulation of air flow into aquifers |
| WO2011045603A1 (en) | 2009-10-15 | 2011-04-21 | Oilflow Solutions Holdings Limited | Hydrocarbons |
| EA015320B1 (en) * | 2003-10-02 | 2011-06-30 | Ойлфлоу Солюшнз Холдингз Лимитед | Method for reducing the viscosity of viscous fluids (embodiments) |
| WO2013017838A1 (en) | 2011-08-01 | 2013-02-07 | Oilflow Solutions Holdings Limited | Enhanced oil recovery |
| US8512576B2 (en) | 2004-05-17 | 2013-08-20 | Caltec Limited | System and method for the production or handling of heavy oil |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB0106195D0 (en) * | 2001-03-14 | 2001-05-02 | Corpro Systems Ltd | Apparatus and method |
| NO315937B1 (en) * | 2001-12-10 | 2003-11-17 | Asbjoern Nes | Silage of grass balls without wrapping in plastic |
| GB0207376D0 (en) * | 2002-03-28 | 2002-05-08 | Advanced Gel Technology Ltd | Recovering materials |
| GB0312781D0 (en) | 2003-06-04 | 2003-07-09 | Ythan Environmental Services L | Method |
| GB2408330B (en) * | 2003-11-22 | 2008-12-03 | Advanced Gel Technology Ltd | Polymeric materials comprising pH indicators for use in wound dressings |
| GB0408145D0 (en) * | 2004-04-13 | 2004-05-19 | Aubin Ltd | Crude oil mobility |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2030575A (en) * | 1978-08-09 | 1980-04-10 | Agency Ind Science Techn | Photosensitive resin and method for manufacture thereof |
| EP0393578A2 (en) * | 1989-04-15 | 1990-10-24 | Nippon Paint Co., Ltd. | Aqueous resin composition |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1211193A (en) * | 1966-07-26 | 1970-11-04 | Nat Res Dev | Polymers of unsymmetrically substituted alkenes |
| US3658771A (en) * | 1969-01-14 | 1972-04-25 | Dow Chemical Co | Preparing ammonium polyacrylates |
| US4039542A (en) * | 1974-05-06 | 1977-08-02 | American Cyanamid Company | Unsaturated pyrimidine |
| JPS584712B2 (en) * | 1979-07-04 | 1983-01-27 | 工業技術院長 | Nitrogen-containing heterocyclic compound having an acetal group and method for producing the same |
| US4276362A (en) * | 1979-09-07 | 1981-06-30 | Catalyst Research Corporation | Depolarizers for lithium halide batteries |
| US4709767A (en) * | 1986-01-06 | 1987-12-01 | American Colloid Company | Production process for manufacturing low molecular weight water soluble acrylic polymers as drilling fluid additives |
| JPS62262457A (en) * | 1986-05-09 | 1987-11-14 | Nippon Oil & Fats Co Ltd | Polymer LB membrane electric device |
| DE3781315T2 (en) * | 1986-05-09 | 1993-03-04 | Nippon Oils & Fats Co Ltd | ULTRADUENNE MEMBRANE OF THE LANGMUIR BLODGETT TYPE MADE OF POLYFUMURATE. |
| US5258473A (en) * | 1989-11-20 | 1993-11-02 | Basf Aktiengesellschaft | Preparation of finely divided, water-soluble polymers |
| JP2723200B2 (en) * | 1992-09-07 | 1998-03-09 | 均 笠井 | Manufacturing method of organic microcrystal for nonlinear optics |
-
1996
- 1996-09-18 GB GBGB9619419.6A patent/GB9619419D0/en active Pending
-
1997
- 1997-09-16 CA CA002266578A patent/CA2266578C/en not_active Expired - Fee Related
- 1997-09-16 BR BR9712059-6A patent/BR9712059A/en not_active IP Right Cessation
- 1997-09-16 AU AU43097/97A patent/AU734288C/en not_active Ceased
- 1997-09-16 RU RU99107383/04A patent/RU2249603C2/en not_active IP Right Cessation
- 1997-09-16 NZ NZ335075A patent/NZ335075A/en unknown
- 1997-09-16 EP EP97919164A patent/EP0935622A1/en not_active Withdrawn
- 1997-09-16 JP JP51439898A patent/JP4159609B2/en not_active Expired - Fee Related
- 1997-09-16 WO PCT/GB1997/002529 patent/WO1998012239A1/en not_active Ceased
- 1997-09-16 CN CN97198022.5A patent/CN1217967C/en not_active Expired - Fee Related
- 1997-09-18 GB GB9719759A patent/GB2317895B/en not_active Expired - Fee Related
-
1999
- 1999-03-16 NO NO19991276A patent/NO991276L/en not_active Application Discontinuation
-
2008
- 2008-02-20 JP JP2008038750A patent/JP2008174756A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2030575A (en) * | 1978-08-09 | 1980-04-10 | Agency Ind Science Techn | Photosensitive resin and method for manufacture thereof |
| EP0393578A2 (en) * | 1989-04-15 | 1990-10-24 | Nippon Paint Co., Ltd. | Aqueous resin composition |
Cited By (29)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7281579B2 (en) * | 2001-12-07 | 2007-10-16 | Aqueolic Canada Ltd. | Method for terminating or reducing water flow in a subterranean formation |
| WO2003083259A2 (en) | 2002-03-28 | 2003-10-09 | Advanced Gel Technology Limited | Recovering materials |
| WO2003102052A1 (en) * | 2002-05-31 | 2003-12-11 | Advanced Gel Technology Limited | Dispersion |
| AU2003273566B2 (en) * | 2002-05-31 | 2009-06-11 | Advanced Gel Technology Limited | Dispersion |
| RU2320680C2 (en) * | 2002-05-31 | 2008-03-27 | Эдвансд Джел Текнолоджи Лимитед | Dispersion |
| US7202300B2 (en) | 2002-05-31 | 2007-04-10 | Advanced Gel Technology Limited | Dispersion |
| GB2428241A (en) * | 2002-11-05 | 2007-01-24 | Univ Bradford | Polymeric material |
| GB2428241B (en) * | 2002-11-05 | 2007-08-15 | Univ Bradford | Polymeric materials |
| WO2004083589A2 (en) | 2003-03-20 | 2004-09-30 | Agt Energy Limited | Restricting fluid passage and novel materials therefor |
| GB2424879A (en) * | 2003-10-02 | 2006-10-11 | Agt Energy Ltd | Cleaning contaminated materials |
| GB2425777B (en) * | 2003-10-02 | 2008-12-17 | Proflux Systems Llp | Viscous fluids |
| GB2423324B (en) * | 2003-10-02 | 2007-04-18 | Agt Energy Ltd | Fracturing of subterranean formations |
| GB2423324A (en) * | 2003-10-02 | 2006-08-23 | Agt Energy Ltd | Fracturing of subterranean formations |
| WO2005040553A1 (en) * | 2003-10-02 | 2005-05-06 | Agt Energy Limited | Fracturing of subterranean formations |
| WO2005040669A1 (en) * | 2003-10-02 | 2005-05-06 | Proflux Systems Llp | Method for reducing the viscosity of viscous fluids |
| GB2424879B (en) * | 2003-10-02 | 2008-04-30 | Agt Energy Ltd | Cleaning contaminated materials |
| EA015320B1 (en) * | 2003-10-02 | 2011-06-30 | Ойлфлоу Солюшнз Холдингз Лимитед | Method for reducing the viscosity of viscous fluids (embodiments) |
| EP2256401A1 (en) | 2003-10-02 | 2010-12-01 | Oilflow Solutions Holdings Limited | Method for reducing the viscosity of viscous fluids |
| GB2425777A (en) * | 2003-10-02 | 2006-11-08 | Proflux Systems Llp | Method for reducing the viscosity of viscous fluids |
| WO2005033469A1 (en) * | 2003-10-02 | 2005-04-14 | Agt Energy Limited | Cleaning contaminated materials |
| US7745500B2 (en) | 2003-10-02 | 2010-06-29 | Advanced Gel Technology Limited | Method for reducing the viscosity of viscous fluids |
| AU2004284273B2 (en) * | 2003-10-02 | 2010-08-26 | Oilflow Solutions Holdings Limited | Method for reducing the viscosity of viscous fluids |
| US8178586B2 (en) | 2003-10-02 | 2012-05-15 | Oilflow Solutions Holdings Limited | Method for reducing the viscosity of viscous fluids |
| US8512576B2 (en) | 2004-05-17 | 2013-08-20 | Caltec Limited | System and method for the production or handling of heavy oil |
| EP2018191A2 (en) * | 2006-05-17 | 2009-01-28 | AGT Sciences Limited | Delivery means |
| WO2008152357A1 (en) | 2007-06-15 | 2008-12-18 | Proflux Systems Llp | Hydrocarbons |
| US7832478B2 (en) | 2007-11-07 | 2010-11-16 | Schlumberger Technology Corporation | Methods for manipulation of air flow into aquifers |
| WO2011045603A1 (en) | 2009-10-15 | 2011-04-21 | Oilflow Solutions Holdings Limited | Hydrocarbons |
| WO2013017838A1 (en) | 2011-08-01 | 2013-02-07 | Oilflow Solutions Holdings Limited | Enhanced oil recovery |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2008174756A (en) | 2008-07-31 |
| RU2249603C2 (en) | 2005-04-10 |
| NZ335075A (en) | 2001-03-30 |
| CN1217967C (en) | 2005-09-07 |
| NO991276D0 (en) | 1999-03-16 |
| AU4309797A (en) | 1998-04-14 |
| BR9712059A (en) | 2000-01-18 |
| CA2266578A1 (en) | 1998-03-26 |
| CN1230970A (en) | 1999-10-06 |
| GB2317895A (en) | 1998-04-08 |
| EP0935622A1 (en) | 1999-08-18 |
| AU734288B2 (en) | 2001-06-07 |
| NO991276L (en) | 1999-05-12 |
| AU734288C (en) | 2003-03-27 |
| GB9619419D0 (en) | 1996-10-30 |
| JP2001500558A (en) | 2001-01-16 |
| JP4159609B2 (en) | 2008-10-01 |
| GB2317895B (en) | 2001-04-11 |
| GB9719759D0 (en) | 1997-11-19 |
| CA2266578C (en) | 2008-12-23 |
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