WO1996016921A1 - A method for inhibiting premature polymerization of vinyl aromatic monomers - Google Patents
A method for inhibiting premature polymerization of vinyl aromatic monomers Download PDFInfo
- Publication number
- WO1996016921A1 WO1996016921A1 PCT/EP1995/004501 EP9504501W WO9616921A1 WO 1996016921 A1 WO1996016921 A1 WO 1996016921A1 EP 9504501 W EP9504501 W EP 9504501W WO 9616921 A1 WO9616921 A1 WO 9616921A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- oxyl
- tetramethylpiperidin
- vinyl aromatic
- bis
- nitroxyl
- Prior art date
Links
- 0 CC(C)(CC*(**(CCCC1(C)C)CC(C)(C)N1O)CC1(C)C)N1O Chemical compound CC(C)(CC*(**(CCCC1(C)C)CC(C)(C)N1O)CC1(C)C)N1O 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/20—Use of additives, e.g. for stabilisation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
- C07B63/00—Purification; Separation; Stabilisation; Use of additives
- C07B63/04—Use of additives
Definitions
- This invention pertains to the compositions, processes and methods of using nitroxyl inhibitors in combination with oxygen, to prevent the premature polymerization of vinyl aromatic monomers.
- vinyl aromatic monomer compounds such as styrene or ⁇ -methyl- styrcne
- Manufacturing processes for such monomers typically include distillations at elevated temperatures.
- polymerization inhibitors include elemental sulfur and many classes of organic chemicals. These materials have met with varying degrees of success in industrial use. Included among these organic materials are nitrated phenol derivatives, C- and N-nitroso compounds and nitroxyl derivatives. A particularly effective class of such inhibitors are hindered amine nitroxyls. This class of stable free radicals is characterized by having a NO* group, where the * asterisk denotes an unpaired electron, and where the nitrogen atom is further flanked by two carbon atoms,- to neither of which hydrogen atoms are attached.
- flanking carbon atoms are further connected by various bridging groups to form cyclic structures, such as, for example, six-membered piperidines, piperazines, five membered pyrollidines and the like.
- cyclic structures such as, for example, six-membered piperidines, piperazines, five membered pyrollidines and the like.
- these stable free nitroxyl radicals also called nitroxides
- hinderedered amine nitroxyl free radicals.
- Compounds of this class are not only valuable inhibitors of free radical-initiated polymerization in unsaturated monomers, but also have found uses as spin labels in biochemical applications.
- Soviet Patent No. 1,027,150 discloses the stabilization of styrene by using nitroxyl radical.
- Soviet Patent No. 1,139,722 discloses the use of a bis-nitroxyl radical as the thermal polymerization inhibitor for styrene.
- Japanese Hei 1-165534 discloses the use of 1-piperidyloxy derivatives as polymerization inhibitors for styrene.
- Soviet Patent No. 1,558,888 discloses the polymerization inhibition of styrene by a nitroxyl radical.
- U.S. Patent No. 3,733,326 discloses the polymerization inhibition of vinyl monomers by free radical precursors.
- One object of the present invention is to provide a composition comprising a vinyl aromatic compound, and an effective amount of nitroxyl inhibitor and oxygen or air to optimize the effectiveness of the inhibitor.
- Another object of the invention is to provide a process for the highly efficient utilization of nitroxyl inhibitors.
- the method of boosting inhibiting activity with air or oxygen is particularly noteworthy and unobvious in view of existing literature indicating that oxygen does catalyze rather than inhibit thermal styrene polymerization (P.D. Bartlett, Angew.Chem., 67, 45-52 (1955), even though oxygen is known to inhibit the polymerization of other monomers such as acrylic monomers.
- the instant invention pertains to a composition which comprises
- the effective amount of nitroxyl compound is, for example, from 1 to 2000 ppm, based on the weight of component (a).
- the amount of nitroxyl compound is from 5 to 1000 ppm, based on the weight of component (a).
- the effective amount of oxygen or air is, for example, 10 ppm to about 1000 ppm, based on the weight of component (a).
- the upper practical limit for this amount will be determined by safety considerations.
- the vinyl aromatic monomer of component (a) is, for example, selected from the group consisting of styrene, ⁇ -methylstyrene, vinyltoluene, divinylbenzene, styrenesulfonic acid and structural isomers, derivatives of said compounds and mixtures thereof.
- the vinyl aromatic monomer is styrene, ⁇ -methylstyrene, vinyltoluene or divinylbenzene; most preferably styrene.
- This invention is applicable to hindered amine nitroxyl radicals in general, i.e. compounds having at least one NO* group, where the * asterisk denotes an unpaired electron, and the nitrogen atom is further flanked by two carbon atoms, to neither of which hydrogen atoms are attached. These flanking carbon atoms may be further connected by various bridging groups to form cyclic structures such as for example six-membered piperidines, piperazines, five membered pyrolidines and the like.
- the hindered amine nitroxyl compounds useful in this invention may, for example, correspond to the generic structure
- each R is alkyl and T is a group required to complete a 5- or 6-membered ring.
- Two or more nitroxyl groups may be present in the same molecule by being linked through the T moiety as exemplified below where E is a linking group.
- hindered amine nitroxyl compounds are those of formulae I to III, in particular formula II, disclosed on page 3 of EP-A-592 363 wherein the hindered N atom bears an -O* radical; as well as those of general formulae IV to X on pages 4 to 21 of EP-A-592363 wherein G 11 is oxyl.
- Non-limiting examples for nitroxyl compounds useful in the present invention are listed below:
- the hindered amine nitroxyl compound of component (b) is bis(l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl) sebacate, l-oxyl-2,2,6,6-tetramethylpiperidine, bis(l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl) n-butylmalonate, bis( 1 -oxyl-2,2,6,6-tetramethylpiperidin-4-yl) succinate, bis(l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl) hexahydroterephthalate, 1 -oxyl-2,2,6,6-tetramethylpiperidin-4-yl 4-tert-butylbenzoate, l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl propionate, or 1 -oxyl-2,2,6,6-tetramethylpiperidin-4-yl benzoate.
- composition may also contain a solvent such as ethylbenzene or contain dissolved polymer such a saturated or unsaturated polyester.
- the instant invention also pertains to a process for inhibiting the premature polymerization of a vinyl aromatic compound during distillation or purification which comprises incorporating therein an effective inhibiting amount, sufficient to prevent premature polymerization during distillation or purification of said vinyl aromatic compound, of a stable hindered nitroxyl compound used together with an effective amount of oxygen or air to enhance the inhibiting activity of the nitroxyl compound.
- the vinyl aromatic compound is distilled or purified at a temperature from 50°C to 150°C. Th stable nitroxyl compound is added to the vinyl aromatic compound continuously or intermittently upstream to the point where distillation or purification occurs; or the stable nitroxyl compound can be added at different entry points into the vinyl aromatic compound process stream prior to the point where distillation or purification occurs.
- the instant process can be started under either anaerobic or aerobic conditions with air or oxygen then being added continuously or intermittently thereafter to the vinyl aromatic monomer to prolong polymerization inhibition time or to short-stop incipient polymerization.
- vinyl aromatic monomer includes any of readily polymerizable vinyl aromatic compounds, e.g. styrene, ⁇ -methylstyrene, vinyltoluene, divinylbenzene, styrenesulfonic acid and structural isomers, and derivatives and mixtures thereof.
- styrene e.g. styrene, ⁇ -methylstyrene, vinyltoluene, divinylbenzene, styrenesulfonic acid and structural isomers, and derivatives and mixtures thereof.
- the preferred compounds and amounts for carrying out the inventive process are as given for the aforementioned inventive composition.
- the effective amount of polymerization inhibitors added may vary over wide ranges depending upon the particular vinyl aromatic compound and the conditions of distillation.
- the total amount of a nitroxyl compound is from 1 ppm to about 2,000 ppm based upon the weight of the monomer being inhibited.
- the inhibitor system is used in the range of 5 to 1,000 ppm.
- the temperature of the reboiler is, generally, in the range of 50°C to about 150°C.
- the polymerization inhibitor can be introduced into the monomer to be protected by any conventional method. It may be added as a concentrate solution in suitable solvents just upstream of the point of desired application by any suitable means.
- the instant invention also pertains to the use of a stable hindered nitroxyl compound together with an effective amount of oxygen or air to enhance the inhibiting activity of the nitroxyl compound for inhibiting the premature polymerization of a vinyl aromatic compound during distillation or purification.
- the preferred compounds and amounts arc as given for the aforementioned inventive composition.
- styrene is freed of tert-butyl catechol storage stabilizer by washing with 1 N sodium hydroxide solution, water and subsequent distillation under reduced pressure.
- a 300 mL 3-necked flask equipped with thermometer, condenser, rubber septum and magnetic stirrer bar is charged with 100 g of styrene, purified as described above, and 50 mg of bis(l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl) sebacate, to give a 500 ppm solution of this representative nitroxyl inhibitor.
- An oxygen-free atmosphere is established by five consecutive evacuations and backfilling with nitrogen, followed by sparging the styrene solution with pure nitrogen for 15 minutes.
- the vessel is immersed into a mechanically stirred and thermostatically controlled oil bath at 120°C. Samples are withdrawn at twenty minute intervals, and the amount of polystyrene formed is then determined by refractive index measurements which in turn are calibrated with authentic polystyrene in styrene solutions of known concentration.
- the onset of polymerization occurs abruptly at the end of a characteristic induction period. The length of this induction period the "inhibition time" is determined experimentally by extrapolating the linear polymer/time curve.
- Example 4-5 no inhibitor is added to the system whether done under nitrogen or under air.
- the polymerization onset occurs after only 6 minutes in each instance, which is the time period required to heat the reaction mass from room temperature to 120°C.
- Example 1 The addition of air is also used as a short-stop of polymerization once polymerization has started under anaerobic conditions.
- the experiment of Example 1 is repeated under strictly anaerobic conditions.
- polymerization starts and is allowed to proceed for ten minutes. This results in a styrene polymer content of 1 %.
- a single addition of 50 mL of air is injected into the solution at a rate of 6 mL/min.
- This air quantity contains 10.5 ml (0.43 mmoles) or 14 mg of oxygen which amounts to 140 ppm of oxygen relative to styrene.
- Example 1 Following the procedure of Example 1 under strictly anaerobic conditions, 541 ppm of l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl benzoate in styrene is heated at 120°C and produces the same inhibition time of 50 minutes as the difunctional inhibitor of Example 1.
- the molar nitroxyl concentration of this monofunctional derivative is the same as the molar nitroxyl group concentration of the difunctional derivative of Example 1.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Water Supply & Treatment (AREA)
- Hydrogenated Pyridines (AREA)
- Polymerisation Methods In General (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
Claims
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
RU97110784A RU2127243C1 (en) | 1995-02-03 | 1995-11-16 | Composition preventing premature polymerization and method of inhibiting premature polymerization |
BR9509777A BR9509777A (en) | 1994-11-28 | 1995-11-16 | Method to inhibit premature polymerization of aromatic vinyl monomers |
EP95940182A EP0794933B1 (en) | 1994-11-28 | 1995-11-16 | A method for inhibiting premature polymerization of vinyl aromatic monomers |
MXPA/A/1997/003906A MXPA97003906A (en) | 1994-11-28 | 1995-11-16 | A method for inhibiting the premature polymerization of aromatic vinyl monomers |
KR1019970703616A KR100248534B1 (en) | 1994-11-28 | 1995-11-16 | A method for inhibiting premature polymerization of vinyl aromatic monomers |
CA002203397A CA2203397C (en) | 1994-11-28 | 1995-11-16 | A method for inhibiting premature polymerization of vinyl aromatic monomers |
DE69514384T DE69514384T2 (en) | 1994-11-28 | 1995-11-16 | METHOD FOR INHIBITING EARLY POLYMERIZATION OF VINYL AROMATIC MONOMERS |
AU41723/96A AU4172396A (en) | 1994-11-28 | 1995-11-16 | A method for inhibiting premature polymerization of vinyl aomatic monomers |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US34509794A | 1994-11-28 | 1994-11-28 | |
US08/383,279 | 1995-02-03 | ||
US08383279 US5545786C1 (en) | 1994-11-28 | 1995-02-03 | Method for inhibiting premature polymerization of vinyl aromatic monomers |
US08/345,097 | 1995-02-03 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1996016921A1 true WO1996016921A1 (en) | 1996-06-06 |
Family
ID=26994252
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP1995/004501 WO1996016921A1 (en) | 1994-11-28 | 1995-11-16 | A method for inhibiting premature polymerization of vinyl aromatic monomers |
Country Status (10)
Country | Link |
---|---|
US (2) | US5545786C1 (en) |
EP (2) | EP0959059A3 (en) |
JP (1) | JP2818977B2 (en) |
KR (1) | KR100248534B1 (en) |
CN (1) | CN1046493C (en) |
AU (1) | AU4172396A (en) |
BR (1) | BR9509777A (en) |
CA (1) | CA2203397C (en) |
DE (1) | DE69514384T2 (en) |
WO (1) | WO1996016921A1 (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0845448A1 (en) * | 1996-12-02 | 1998-06-03 | Ciba SC Holding AG | Inhibiting polymerization of vinyl aromatic monomers |
WO1998058038A1 (en) * | 1997-06-17 | 1998-12-23 | Basf Aktiengesellschaft | Mixture of substances containing compounds with vinyl groups and stabilizers |
EP0963971A1 (en) * | 1998-06-10 | 1999-12-15 | Nalco/Exxon Energy Chemicals L.P. | Method for inhibiting polymer formation in styrene processing |
ES2142274A1 (en) * | 1997-03-20 | 2000-04-01 | Coba Especialty Chemicals Hold | Inhibition of polymerization |
WO2000036052A1 (en) * | 1998-12-17 | 2000-06-22 | Nalco/Exxon Energy Chemicals, L.P. | Inhibiting polymerization of vinyl aromatic monomers using synergistic mixtures containing nitroxide stabilizers |
WO2000076943A1 (en) * | 1999-06-11 | 2000-12-21 | Basf Aktiengesellschaft | Method for preventing undesired polymerisation in a mixture of substances containing ethylenically unsaturated compounds |
US6200460B1 (en) | 1996-12-10 | 2001-03-13 | Basf Aktiengesellschaft | Substance mixtures containing stabilizers and compounds containing vinyl groups |
US7029556B1 (en) * | 1999-11-24 | 2006-04-18 | Arkema | Method for purifying (meth)acrylic monomers by distillation |
WO2014151254A1 (en) * | 2013-03-15 | 2014-09-25 | Bausch & Lomb Incorporated | Method and apparatus for delaying polymerisation |
US8968611B2 (en) | 2008-06-09 | 2015-03-03 | Adeka Corporation | Process for solidification of phosphoric ester-based flame retardants |
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US6409887B1 (en) | 1996-07-15 | 2002-06-25 | Aah Marks And Company Limited | Polymerization inhibitor |
WO1998014416A1 (en) * | 1996-10-04 | 1998-04-09 | Betzdearborn Inc. | Compositions and methods for inhibiting vinyl aromatic monomer polymerization |
US5928558A (en) * | 1997-06-13 | 1999-07-27 | Ciba Specialty Chemicals Corporation | Derivatives of 1-oxyl-4-amino-2,2,6,6-tetramethylpiperidine as polymerization inhibitors for (meth)acrylate monomers |
US6024894A (en) * | 1998-03-25 | 2000-02-15 | Betzdearborn Inc. | Compositions and methods for inhibiting vinyl aromatic monomer polymerization |
US5907071A (en) * | 1998-04-21 | 1999-05-25 | Betzdearborn Inc. | Compositions and methods for inhibiting vinyl aromatic monomer polymerization |
EP1095006B1 (en) | 1998-07-14 | 2008-12-24 | Ciba Holding Inc. | Derivatives of 1-oxyl-4-hydroxy-2,2,6,6-tetramethylpiperidine as polymerization inhibitors for (meth) acrylate monomers |
KR20010079775A (en) * | 1998-09-09 | 2001-08-22 | 칼 에이. 로월드 | Styrene monomer polymerization inhibition using substituted dihydroxyarenes and nitroxides |
US20040019247A1 (en) * | 1999-02-26 | 2004-01-29 | Basf Aktiengesellschaft | Continuous recovery of styrene from a styrene-containing mixture |
US6300533B1 (en) | 1999-08-16 | 2001-10-09 | Uniroyal Chemical Company, Inc. | Inhibition of polymerization of ethylenically unsaturated monomers |
ATE307789T1 (en) * | 1999-12-02 | 2005-11-15 | Crompton Corp | POLYMERIZATION INHIBITION OF UNSATURATED MONOMERS |
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US20050192384A1 (en) * | 1999-12-09 | 2005-09-01 | Tunja Jung | Additive composition for increasing the storage stability of ethylenically unsaturated resins |
US20110071232A1 (en) * | 1999-12-09 | 2011-03-24 | Tunja Jung | Additive composition for increasing the storage stability of ethylenically unsaturated resins |
US6403850B1 (en) | 2000-01-18 | 2002-06-11 | Uniroyal Chemical Company, Inc. | Inhibition of polymerization of unsaturated monomers |
US6344560B1 (en) | 2000-05-03 | 2002-02-05 | Uniroyal Chemical Company, Inc. | Nitroaromatic solubilizer for nitroxyls in aromatic solvents |
US6376728B1 (en) | 2000-06-20 | 2002-04-23 | Hercules Incorporated | Method, composition and mixture for inhibiting monomer polymerization |
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US6685823B2 (en) * | 2000-10-16 | 2004-02-03 | Uniroyal Chemical Company, Inc. | C-nitrosoaniline compounds and their blends as polymerization inhibitors |
WO2002033026A1 (en) | 2000-10-16 | 2002-04-25 | Uniroyal Chemical Company, Inc. | Blends of quinone alkide and nitroxyl compounds as polymerization inhibitors |
US7125475B2 (en) * | 2002-02-15 | 2006-10-24 | Crompton Corporation | Nitrosophenols and C-nitrosoanilines as polymerization inhibitors |
US20060069219A1 (en) * | 2004-09-28 | 2006-03-30 | Vilan Kosover | Sulfonated phenols with nitrophenols as polymerization inhibitors |
US7691952B2 (en) * | 2004-09-28 | 2010-04-06 | Chemtura Corporation | Sulfonated nitrophenols as polymerization inhibitors |
US7696290B2 (en) * | 2004-12-03 | 2010-04-13 | Crompton Corporation | Aromatic sulfonic acids, amines, and nitrophenols in combination with nitroxyl radical-containing compounds or C-nitrosanilines as polymerization inhibitors |
EP1843995B1 (en) | 2005-02-04 | 2013-06-05 | Chemtura Corporation | Means for controlling the exothermic reaction of styrenic monomers with sulfonic acids |
US7553896B2 (en) * | 2005-06-17 | 2009-06-30 | Chemtura Corporation | Ortho-nitrosophenols as polymerization inhibitors |
EP1978017A4 (en) | 2005-12-27 | 2011-01-26 | Adeka Corp | Nitroxyl compound, and polymerization inhibitor and polymerization inhibitor composition using same |
JP5105762B2 (en) * | 2006-04-12 | 2012-12-26 | 日本合成化学工業株式会社 | Method for inhibiting polymerization of vinyl carboxylate |
DE102007023515A1 (en) * | 2006-07-05 | 2008-01-10 | Evonik Degussa Gmbh | Preparing 1,7-diolefin, useful to prepare alpha, omega-diamine, -diol and sebacic acid, comprises hydrodimerization of non-cyclic olefins with two conjugated double bonds in the presence of a reducing agent and a catalyst |
US7968001B2 (en) | 2007-12-19 | 2011-06-28 | Air Products And Chemicals, Inc. | Stabilizers for the stabilization of unsaturated hydrocarbon-based precursor |
US8440099B2 (en) | 2007-12-19 | 2013-05-14 | Air Products And Chemicals, Inc. | Stabilizers for the stabilization of unsaturated hydrocarbon-based precursor |
EP2072485B1 (en) * | 2007-12-19 | 2012-06-20 | Air Products and Chemicals, Inc. | Stabilizers for the stabilization of unsaturated hydrocarbon-based precursor |
US8716502B2 (en) * | 2010-12-17 | 2014-05-06 | Dow Global Technologies Llc | Process for preparing divinylarene oxides |
CA2857384C (en) * | 2011-11-29 | 2016-08-16 | Dorf Ketal Chemicals (India) Private Limited | Amine based additive composition for control and inhibition of polymerization of styrene, and method of use thereof |
JP6176420B2 (en) * | 2015-07-01 | 2017-08-09 | Dic株式会社 | Stabilizer compound, liquid crystal composition, and display element |
ES2870125T3 (en) * | 2017-03-09 | 2021-10-26 | Ecolab Usa Inc | Polymerization Inhibitor Compositions |
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1995
- 1995-02-03 US US08383279 patent/US5545786C1/en not_active Expired - Fee Related
- 1995-05-17 US US08443051 patent/US5545782C1/en not_active Expired - Fee Related
- 1995-11-16 DE DE69514384T patent/DE69514384T2/en not_active Revoked
- 1995-11-16 WO PCT/EP1995/004501 patent/WO1996016921A1/en not_active Application Discontinuation
- 1995-11-16 CN CN95196481A patent/CN1046493C/en not_active Expired - Fee Related
- 1995-11-16 EP EP99112035A patent/EP0959059A3/en not_active Withdrawn
- 1995-11-16 JP JP8518128A patent/JP2818977B2/en not_active Expired - Fee Related
- 1995-11-16 EP EP95940182A patent/EP0794933B1/en not_active Revoked
- 1995-11-16 KR KR1019970703616A patent/KR100248534B1/en not_active IP Right Cessation
- 1995-11-16 CA CA002203397A patent/CA2203397C/en not_active Expired - Fee Related
- 1995-11-16 AU AU41723/96A patent/AU4172396A/en not_active Abandoned
- 1995-11-16 BR BR9509777A patent/BR9509777A/en not_active Application Discontinuation
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Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0845448A1 (en) * | 1996-12-02 | 1998-06-03 | Ciba SC Holding AG | Inhibiting polymerization of vinyl aromatic monomers |
US6117276A (en) * | 1996-12-02 | 2000-09-12 | Nalco/Exxon Energy Chemicals, L.P. | Inhibiting polymerization of vinyl aromatic monomers |
US6200460B1 (en) | 1996-12-10 | 2001-03-13 | Basf Aktiengesellschaft | Substance mixtures containing stabilizers and compounds containing vinyl groups |
ES2142274A1 (en) * | 1997-03-20 | 2000-04-01 | Coba Especialty Chemicals Hold | Inhibition of polymerization |
JP2002504128A (en) * | 1997-06-17 | 2002-02-05 | ビーエーエスエフ アクチェンゲゼルシャフト | Mixture containing a compound having a vinyl group and a stabilizer |
WO1998058038A1 (en) * | 1997-06-17 | 1998-12-23 | Basf Aktiengesellschaft | Mixture of substances containing compounds with vinyl groups and stabilizers |
US6475348B1 (en) | 1997-06-17 | 2002-11-05 | Basf Aktiengesellschaft | Mixture of substances containing compounds with vinyl groups and stabilizers |
EP0963971A1 (en) * | 1998-06-10 | 1999-12-15 | Nalco/Exxon Energy Chemicals L.P. | Method for inhibiting polymer formation in styrene processing |
WO2000036052A1 (en) * | 1998-12-17 | 2000-06-22 | Nalco/Exxon Energy Chemicals, L.P. | Inhibiting polymerization of vinyl aromatic monomers using synergistic mixtures containing nitroxide stabilizers |
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US6835288B1 (en) | 1999-06-11 | 2004-12-28 | Basf Aktiengesellschaft | Method for preventing undesired polymerization in a mixture of substances containing ethylenically unsaturated compounds |
US7029556B1 (en) * | 1999-11-24 | 2006-04-18 | Arkema | Method for purifying (meth)acrylic monomers by distillation |
US8968611B2 (en) | 2008-06-09 | 2015-03-03 | Adeka Corporation | Process for solidification of phosphoric ester-based flame retardants |
WO2014151254A1 (en) * | 2013-03-15 | 2014-09-25 | Bausch & Lomb Incorporated | Method and apparatus for delaying polymerisation |
AU2014235179B2 (en) * | 2013-03-15 | 2016-02-18 | Bausch & Lomb Incorporated | Method and apparatus for delaying polymerisation |
AU2014235179C1 (en) * | 2013-03-15 | 2016-06-16 | Bausch & Lomb Incorporated | Method and apparatus for delaying polymerisation |
US11414501B2 (en) | 2013-03-15 | 2022-08-16 | Bausch & Lomb Incorporated | Method and apparatus for delaying polymerisation |
Also Published As
Publication number | Publication date |
---|---|
US5545786A (en) | 1996-08-13 |
MX9703906A (en) | 1998-05-31 |
CA2203397C (en) | 2002-01-22 |
US5545782A (en) | 1996-08-13 |
DE69514384T2 (en) | 2000-08-10 |
CN1046493C (en) | 1999-11-17 |
EP0794933B1 (en) | 2000-01-05 |
JP2818977B2 (en) | 1998-10-30 |
CN1166820A (en) | 1997-12-03 |
EP0959059A2 (en) | 1999-11-24 |
EP0794933A1 (en) | 1997-09-17 |
CA2203397A1 (en) | 1996-06-06 |
EP0959059A3 (en) | 1999-12-01 |
AU4172396A (en) | 1996-06-19 |
JPH10504317A (en) | 1998-04-28 |
US5545786C1 (en) | 2001-10-16 |
BR9509777A (en) | 1997-09-30 |
KR100248534B1 (en) | 2000-03-15 |
DE69514384D1 (en) | 2000-02-10 |
US5545782C1 (en) | 2001-05-01 |
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