WO2016172076A1 - Sterically hindered hydroquinones as antifoulants for unsaturated monomers - Google Patents
Sterically hindered hydroquinones as antifoulants for unsaturated monomers Download PDFInfo
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- WO2016172076A1 WO2016172076A1 PCT/US2016/028239 US2016028239W WO2016172076A1 WO 2016172076 A1 WO2016172076 A1 WO 2016172076A1 US 2016028239 W US2016028239 W US 2016028239W WO 2016172076 A1 WO2016172076 A1 WO 2016172076A1
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- tetramethylpiperidine
- oxide
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- 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
- C09K15/00—Anti-oxidant compositions; Compositions inhibiting chemical change
- C09K15/04—Anti-oxidant compositions; Compositions inhibiting chemical change containing organic compounds
- C09K15/30—Anti-oxidant compositions; Compositions inhibiting chemical change containing organic compounds containing heterocyclic ring with at least one nitrogen atom as ring member
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- 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
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- 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
- C08F2/38—Polymerisation using regulators, e.g. chain terminating agents, e.g. telomerisation
- C08F2/42—Polymerisation using regulators, e.g. chain terminating agents, e.g. telomerisation using short-stopping agents
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- 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
- C09K15/00—Anti-oxidant compositions; Compositions inhibiting chemical change
- C09K15/04—Anti-oxidant compositions; Compositions inhibiting chemical change containing organic compounds
Definitions
- the present invention generally relates to compounds and methods for inhibiting the free radical polymerization of unsaturated compounds, particularly vinyl monomers. More particularly, it relates to the use of sterically hindered hydroquinone compounds to inhibit the polymerization of unsaturated compounds such as vinyl monomers that are constituents of hydrocarbon streams.
- Unsaturated compounds can undesirably polymerize at various stages of their manufacture, processing, handling, storage, and use.
- Vinyl monomers can undergo self-initiated polymerization at elevated temperatures even in the absence of polymerization promoters.
- undesired thermal polymerization can be a problem during the purification of vinylic monomers and during sudden process shutdowns.
- Undesirable polymerization results in product loss because the valuable monomer end product is consumed in an undesired side reaction.
- unwanted polymerization results in the precipitation and deposition of polymer foulants on the process equipment thereby reducing production efficiency. Unless the unwanted polymerization is effectively controlled, this fouling of process equipment may require a shutdown of the process so as to remove the undesired polymer by physical methods. This problem is particularly acute in the manufacture and purification of vinyl aromatic monomers.
- DNP dinitrophenols
- DNBP 2,4-dinitro- seobutylphenol
- DNBP 2,4-dinitro- seobutylphenol
- a prime example is Europe's REACH legislation.
- Another equally significant disadvantage is that the DNP compounds release NOx emissions during incineration. As a consequence of these disadvantages, there is a need for antipolymerant compounds that are as efficient as DNBP at reducing polymerization and yet are safe and environmentally friendly.
- the present invention reveals a method for mitigating unwanted polymerization and subsequent fouling of equipment during the processing, transportation, or storage of hydrocarbon streams containing an unsaturated hydrocarbon whereby said streams are contacted with an effective amount of a hydroquinone compound of Formula 1:
- Ri, R2, and R3 are independently hydrogen, alkyl, aryl, heterocyclo, or Ri and R2 together with the carbons they are attached to form a 5- or 6- membered fused cyclo, aryl, heterocyclo, or heteroaryl ring; wherein at least two of Ri, R2, and R3 are other than hydrogen.
- Figure 1 is a graph of the percent polymer formed versus time for various polymerization inhibitors including 2,3,5-trimethyl hydroquinone (TMHQ), 4-hydroxy- 2,2,6,6-tetramethyl-l-piperidinyloxy (HTEMPO), and a combination of TMHQ and HTEMPO.
- TMHQ 2,3,5-trimethyl hydroquinone
- HTEMPO 4-hydroxy- 2,2,6,6-tetramethyl-l-piperidinyloxy
- HTEMPO 4-hydroxy- 2,2,6,6-tetramethyl-l-piperidinyloxy
- the present invention is directed to methods of the use of sterically hindered hydroquinone compounds for inhibiting polymerization of unsaturated compounds like styrene, acrylic acid and its ester, methacrylic acid and esters thereof, and acrylamides, which are prone to premature polymerization of unsaturated carbon-carbon bonds.
- the unsaturated compound is in contact with an effective amount of a hydroquinone compound of Formula 1.
- the unsaturated compounds have high polymerization reactivity rates such that they readily polymerize under typical processing conditions.
- the undesired polymerization of the unsaturated compounds is costly due to the reduction of the desired monomer produced.
- the resultant polymer precipitates out and gets deposited on the process equipment as a foulant.
- the deposited foulant reduces the efficiency of the process such that shutting down the process to physically clean the fouled equipment becomes needed. Physically cleaning equipment is quite costly. Thus, methods for preventing fouling caused by this unwanted
- polymerization are beneficial for many hydrocarbon processes laden with vinylic species.
- One aspect of the invention is a method for preventing fouling during purification, transportation, or storage of a hydrocarbon stream containing a species that have reactive unsaturated carbon-carbon bonds whereby said species is in contact with an effective amount of a hydroquinone compound of Formula 1
- Ri, R2, and R 3 are independently hydrogen, alkyl, aryl, heterocyclo, or Ri and R2 together with the carbons they are attached to form a 5- or 6- membered fused cyclo, aryl, heterocyclo, or heteroaryl ring; wherein at least two of Ri, R2, and R 3 are other than hydrogen.
- Xi, X 2 , and X3 are independently -0-, -S-, -N(R 4 )-, or -C(H)(R 4 )-;
- Zi, Z2, Z 3 , and Z 4 are independently -0-, -S-, -N(R 4 )-, or -C(H)(R 4 )-;
- R 3 is hydrogen, alkyl, aryl, or heterocyclo and;
- R 4 is independently hydrogen, alkyl, aryl, or heterocyclo.
- Xi, X 2 , and X 3 can independently be -O- or -C(H)(R 4 )-, wherein at least one of Xi, X 2 , and X 3 is -C(H)(R 4 )-.
- Z, Z2, Z 3 , and Z 4 can independently be -O- or -C(H)(R 4 )- and wherein at least two of Zi, Z 2 , Z 3 , and Z 4 is -C(H)(R 4 )-.
- Xi, X 2 , and X 3 can independently be -C(H)(R 4 )-, wherein R 4 is hydrogen.
- R 4 is hydrogen.
- Zi, Z 2 , Z 3 , and Z 4 can independently be-C(H)(R 4 )-, wherein R ⁇ is hydrogen.
- Ri, R2, and R 3 can be independently alkyl.
- Ri, R2, and R 3 can be independently methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, or octyl. More preferably, for the compounds of Formula 1, Ri, R2, and R 3 can be independently methyl, ethyl, propyl, or butyl. Most preferably, Ri, R2, and R 3 can be methyl.
- the methods described herein can be used for hydrocarbon streams containing ethylene, propylene, acetylene, styrene, butadiene, or a combination thereof.
- the methods can comprise contacting the hydrocarbon stream with a nitroxide compound in combination with the hydroquinone compounds of Formula 1.
- the nitroxide compounds used in combination with the hydroquinone compound of Formula 1 can be 2,2,6,6-tetramethylpiperidine-l-oxide, 4-hydroxy-2,2,6,6- tetramethylpiperidine- 1 -oxide, 4-methoxy-2,2,6,6-tetramethylpiperidine- 1-oxide, 4- ethoxy-2,2,6,6-tetramethylpiperidine- 1-oxide, 4-propoxy-2,2,6,6-tetramethylpiperidine-l- oxide, 4-butoxy-2,2,6,6-tetramethylpiperidine- 1-oxide, or a combination thereof.
- the nitroxide compound can be 2,2,6,6-tetramethylpiperidine- 1-oxide, 4- hydroxy-2,2,6,6-tetramethylpiperidine- 1-oxide, 4-butoxy-2,2,6,6-tetramethylpiperidine-l- oxide, or a combination thereof. More preferably, the nitroxide compound comprises 4- hydroxy-2,2,6,6-tetramethylpiperidine- 1 -oxide.
- the polymerization inhibition method can also prevent unwanted polymerization and the fouling of the process equipment in a primary fractionation process, light ends fractionation, non-aromatic halogenated vinyl fractionation, process- gas compression, dilution steam system, caustic tower, quench water tower, butadiene extraction, propane dehydrogenation, diesel and petrol fuel stabilization, olefin metathesis, styrene purification, hydroxyhydrocarbon purification, or delays the polymerization of resins and compositions comprising ethylenically unsaturated species.
- the polymerization inhibition method can prevent fouling due to the polymerization of the unsaturated and reactive compounds in the butadiene extraction or styrene purification processes.
- Another aspect of the invention is a composition comprising a compound of Formula 1 and a solvent.
- Suitable organic solvents include, and are not limited to, pentane, heptane, hexane, benzene, ethylbenzene, toluene, or a combination thereof.
- the composition can comprise one or more additional polymerization inhibitors.
- Compounds that are suitable as additional polymerization inhibitors in the inventive composition include phenols, alkylated phenols, nitrophenols, nitrosophenols, quinones, hydroquinones, quinone ethers, quinone methides, amines, hydroxylamines, and phenothiazines.
- composition comprising the compound of Formula 1 and a solvent can further comprise a nitroxide compound.
- This nitroxide compound can be 2,2,6,6-tetramethylpiperidine-l-oxide, 4-hydroxy-2,2,6,6-tetramethylpiperidine-l -oxide, 4-methoxy-2,2,6,6-tetramethylpiperidine-l-oxide, 4-ethoxy-2,2,6,6-tetramethylpiperidine- 1-oxide, 4-propoxy-2,2,6,6-tetramethylpiperidine-l -oxide, 4-butoxy-2,2,6,6- tetramethylpiperidine- 1 -oxide, or a combination thereof.
- the nitroxide compound can be 2,2,6,6-tetramethylpiperidine- 1-oxide, 4-hydroxy-2,2,6,6- tetramethylpiperidine- 1-oxide, 4-butoxy-2,2,6,6-tetramethylpiperidine- 1-oxide, or a combination thereof. More preferably, the nitroxide compound comprises 4-hydroxy- 2,2,6,6-tetramethylpiperidine- 1-oxide.
- the polymerization inhibitor compositions described herein can be introduced into the monomer to be protected by any conventional method. It can be added as a concentrate solution in suitable solvents just upstream of the point of desired application by suitable means. In addition, these compounds can be injected separately into the distillation train with the incoming feed, or through separate entry points providing efficient distribution of the inhibitor composition. Since the inhibitor is gradually depleted during operation, it is generally necessary to maintain the appropriate amount of the inhibitor in the distillation apparatus by adding inhibitor during the course of the distillation process. This addition may be carried out either on a generally continuous basis or by intermittently charging inhibitor into the distillation system if the concentration of inhibitor is to be maintained above the minimum required level.
- the effective amount of a compound of Formulae 1, 2, and 3 can be from about 0.1 mmolal to 5 mmolal, from about 0.1 mmolal to 4 mmolal, from about 0.1 mmolal to 3 mmolal, from about 0.1 mmolal to 2 mmolal, from about 0.2 mmolal to 5 mmolal, from about 0.2 mmolal to 4 mmolal, from about 0.2 mmolal to 3 mmolal;
- an alkyl group as described herein alone or as part of another group is an optionally substituted linear saturated monovalent hydrocarbon substituent containing from one to sixty carbon atoms and preferably one to thirty carbon atoms in the main chain or eight to thirty carbon atoms in the main chain, or an optionally substituted branched saturated monovalent hydrocarbon substituent containing three to sixty carbon atoms, and preferably eight to thirty carbon atoms in the main chain.
- unsubstituted alkyl groups include methyl, ethyl, n-propyl, i-propyl, n-butyl, i-butyl, s-butyl, t-butyl, n-pentyl, i-pentyl, s-pentyl, t-pentyl, and the like.
- Cycloalkyl refers to cyclic alkyl groups of from 3 to 10 carbon atoms having single or multiple cyclic rings including fused, bridged, and spiro ring systems.
- suitable cycloalkyl groups include, for instance, adamantyl, cyclopropyl, cyclobutyl, cyclopentyl, cyclooctyl, bicyclo[2.2.2]octanyl and the like.
- Representative cycloalkyl groups include cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl,
- heteroaryl refers to a monocyclic, bicyclic, or tricyclic aromatic heterocyclic group containing one or more heteroatoms (e.g., 1 to 3 heteroatoms) selected from O, S and N in the ring(s).
- Heteroaryl groups include, but are not limited to, pyridyl, pyrazinyl, pyrimidinyl, pyridazinyl, thienyl, furyl, imidazolyl, pyrrolyl, oxazolyl (e.g., 1,3-oxazolyl, 1,2-oxazolyl), thiazolyl (e.g., 1,2-thiazolyl, 1,3- thiazolyl), pyrazolyl, tetrazolyl, triazolyl (e.g., 1,2,3-triazolyl, 1,2,4-triazolyl), oxadiazolyl (e.g., 1,2,3-oxadiazolyl), thiadiazolyl (e.g., 1,3,4-thiadiazolyl), quinolyl, isoquinolyl, benzothienyl, benzofuryl, and indolyl. Heteroaryl groups can be unsubstituted
- heterocyclo refers to a monocyclic, bicyclic, or tricyclic group containing 1 to 4 heteroatoms selected from N, O, S(0) n , P(0) n , PR Z , NH or NR Z , wherein R z is a suitable substituent.
- Heterocyclic groups optionally contain one or two double bonds.
- Heterocyclic groups include, but are not limited to, azetidinyl, tetrahydrofuranyl, imidazolidinyl, pyrrolidinyl, piperidinyl, piperazinyl, oxazolidinyl, thiazolidinyl, pyrazolidinyl, thiomorpholinyl, tetrahydrothiazinyl, tetrahydro-thiadiazinyl, morpholinyl, oxetanyl, tetrahydrodiazinyl, oxazinyl, oxathiazinyl, indolinyl, isoindolinyl, quinuclidinyl, chromanyl, isochromanyl, and benzoxazinyl.
- Examples of monocyclic saturated or partially saturated ring systems are tetrahydrofuran-2-yl, tetrahydrofuran-3-yl, imidazolidin-l-yl, imidazolidin-2-yl, imidazolidin-4-yl, pyrrolidin-l-yl, pyrrolidin-2-yl, pyrrolidin-3-yl, piperidin-l-yl, piperidin-2-yl, piperidin-3-yl, piperazin-l-yl, piperazin-2-yl, piperazin-3-yl, 1,3- oxazolidin-3-yl, isothiazolidine, l,3-thiazolidin-3-yl, 1 ,2-pyrazolidin-2-yl, 1,3-pyrazolidin- 1-yl, thiomorpholin-yl, l,2-tetrahydrothiazin-2-yl, l,3-tetrahydrothiazin-3-yl
- Heterocyclic groups can be unsubstituted or substituted by one or more suitable substituents, preferably 1 to 3 suitable substituents, as defined above.
- aryl or “ar” as used herein alone or as part of another group denote optionally substituted homocyclic aromatic groups, preferably monocyclic or bicyclic groups containing from 6 to 12 carbons in the ring portion, such as phenyl, biphenyl, naphthyl, substituted phenyl, substituted biphenyl or substituted naphthyl. Phenyl and substituted phenyl are the more preferred aryl.
- aryl also includes heteroaryl.
- substituted as in "substituted aryl,” “substituted alkyl,” and the like, means that in the group in question (i.e., the alkyl, aryl or other group that follows the term), at least one hydrogen atom bound to a carbon atom is replaced with one or more substituent groups such as hydroxy (-OH), alkylthio, phosphino, amido (-CON(RAXRB), wherein RA and RB are independently hydrogen, alkyl, or aryl), amino(-N(RA)(RB), wherein RA and RB are independently hydrogen, alkyl, or aryl), halo (fluoro, chloro, bromo, or iodo), silyl, nitro (-N0 2 ), an ether (-ORA wherein RA is alkyl or aryl), an ester (- OC(0)RA wherein RA is alkyl or aryl), keto (-C(O)RA
- substituted introduces a list of possible substituted groups, it is intended that the term apply to every member of that group. That is, the phrase “optionally substituted alkyl or aryl” is to be interpreted as “optionally substituted alkyl or optionally substituted aryl.”
- Alkaryl means an aryl group attached to the parent molecule through an alkylene group.
- the number of carbon atoms in the aryl group and the alkylene group is selected such that there is a total of about 6 to about 18 carbon atoms in the alkaryl group.
- a preferred alkaryl group is benzyl.
- Vinyl monomer refers to a monomer comprising at least one carbon- carbon double bond.
- the monomer can be substituted with various groups, such as acids (e.g., acrylic acid), esters (e.g., acrylate esters), halogen (e.g., vinyl chloride), aryl (e.g., styrene, vinyl toluene, divinylbenzene), cyano (e.g., acrylonitrile), and acetoxy (e.g., vinyl acetate).
- the monomer can be conjugated (e.g., butadiene, cyclopentadiene, vinyl acetylene, indene, and the like).
- a polymerization "inhibitor” refers to a composition of matter that is able to scavenge radicals in a radical polymerization process. Inhibitors can be used to stabilize monomers and prevent their polymerization or quench polymerization when a desired conversion is achieved. They can also be used to regulate or control the kinetics of a polymerization process.
- TMHQ The antipolymerant performance of TMHQ was determined using the static method in which a 0.31 mM solution of the antipolymerant was prepared in inhibitor-free styrene.
- a solution comprising 0.31 mM of TMHQ was prepared by dissolving 0.0179 g the in freshly de-inhibited styrene 350 g of solution.
- FETFE fluoroelastomer
- Dissolved oxygen was purged out of the solutions by sparging with nitrogen for 2 minutes. Once sparged, each tube was immediately sealed and the solution kept under a nitrogen headspace. The tubes were loaded into a heating block that had been preheated to 120 °C. After 30 minutes, and every 15 minutes thereafter, four tubes were retrieved from the block and the polymerization reaction quenched by cooling in an ice bath. The cooled polymer solutions were immediately diluted with toluene.
- TMHQ 0.0090g
- HTEMPO 0.0100 g
- HTEMPO 4-hydroxy-2,2,6,6-i ⁇ ?ira-methylpiperidinoxy
- HTEMPO (0.0199 g) was dissolved in de-inhibited styrene to give a 0.33 mM solution. Using the procedure in Example 1 , the antipolymerant activity of HTEMPO was determined.
- Example 4 Untreated Styrene
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Priority Applications (9)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP16783672.5A EP3289046A4 (en) | 2015-04-20 | 2016-04-19 | Sterically hindered hydroquinones as antifoulants for unsaturated monomers |
| JP2017554871A JP6843067B2 (ja) | 2015-04-20 | 2016-04-19 | 不飽和モノマー類の重合を阻害する方法 |
| CA2982465A CA2982465C (en) | 2015-04-20 | 2016-04-19 | Sterically hindered hydroquinones as antifoulants for unsaturated monomers |
| CN201680022901.8A CN107532083A (zh) | 2015-04-20 | 2016-04-19 | 位阻氢醌作为防污剂用于不饱和单体 |
| RU2017139281A RU2746125C2 (ru) | 2015-04-20 | 2016-04-19 | Пространственно затрудненные гидрохиноны в качестве средств, предохраняющих от обрастания, в отношении ненасыщенных мономеров |
| BR112017022431-3A BR112017022431B1 (pt) | 2015-04-20 | 2016-04-19 | Método para inibir polimerização durante refino, transporte ou armazenamento de uma corrente de hidrocarboneto |
| EP25182651.7A EP4628479A2 (en) | 2015-04-20 | 2016-04-19 | Sterically hindered hydroquinones as antifoulants for unsaturated monomers |
| KR1020177031676A KR102616836B1 (ko) | 2015-04-20 | 2016-04-19 | 불포화 단량체에 대한 방오제로서의 입체 장애 하이드로퀴논 |
| SA517390157A SA517390157B1 (ar) | 2015-04-20 | 2017-10-15 | مركبات هيدروكينون معوَّقة فراغيًا كمضادات اتساخ لمونومرات غير مشبعة |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201562150022P | 2015-04-20 | 2015-04-20 | |
| US62/150,022 | 2015-04-20 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2016172076A1 true WO2016172076A1 (en) | 2016-10-27 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2016/028239 Ceased WO2016172076A1 (en) | 2015-04-20 | 2016-04-19 | Sterically hindered hydroquinones as antifoulants for unsaturated monomers |
Country Status (12)
| Country | Link |
|---|---|
| US (1) | US10155705B2 (enExample) |
| EP (2) | EP3289046A4 (enExample) |
| JP (1) | JP6843067B2 (enExample) |
| KR (1) | KR102616836B1 (enExample) |
| CN (1) | CN107532083A (enExample) |
| AR (1) | AR104327A1 (enExample) |
| BR (1) | BR112017022431B1 (enExample) |
| CA (1) | CA2982465C (enExample) |
| RU (1) | RU2746125C2 (enExample) |
| SA (1) | SA517390157B1 (enExample) |
| TW (1) | TWI624480B (enExample) |
| WO (1) | WO2016172076A1 (enExample) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3763779A1 (en) | 2019-07-09 | 2021-01-13 | SK Innovation Co., Ltd. | Lubricant composition and method of preparing copolymer using the same |
| EP3868792A1 (en) | 2020-02-20 | 2021-08-25 | SK Innovation Co., Ltd. | Method of producing ethylene-carboxylic acid compolymer |
| US11180578B2 (en) | 2018-07-13 | 2021-11-23 | Ecolab Usa Inc. | Polymerization inhibitor and retarder compositions with amine stabilizer |
| US11396629B2 (en) | 2019-10-11 | 2022-07-26 | Ecolab Usa Inc. | Quinone methide and ammonium salt antipolymerant composition and method |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI826485B (zh) | 2018-07-13 | 2023-12-21 | 美商藝康美國公司 | 作為乙烯系單體之防垢劑之含氧胺及醌甲基化物之組合物 |
| CN112739725B (zh) | 2018-09-28 | 2023-09-26 | 埃科莱布美国股份有限公司 | 氨基醌抗聚合剂及其使用方法 |
| ES3002772T3 (en) * | 2018-12-20 | 2025-03-07 | Ecolab Usa Inc | Hydroxylated quinone antipolymerants and methods of using |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5221498A (en) * | 1991-07-22 | 1993-06-22 | Betz Laboratories, Inc. | Methods and compositions for inhibitoring polymerization of vinyl monomers |
| WO2001040404A1 (en) * | 1999-12-03 | 2001-06-07 | Uniroyal Chemical Company, Inc. | Composition and method for inhibiting polymerization and polymer growth |
| WO2006078123A1 (en) * | 2005-01-18 | 2006-07-27 | Yeochun Ncc Co., Ltd. | Polymerization inhibitor for 1,3-butadiene and a method of inhibiting polymerization of 1,3-butadiene by imputing thereof |
Family Cites Families (57)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2455745A (en) | 1943-11-19 | 1948-12-07 | Olin Mathieson | Stabilization of styrene and polymerizable ring chlorinated styrenes |
| US2783271A (en) | 1954-06-29 | 1957-02-26 | Allied Chem & Dye Corp | Continuous production of methacrylic acid esters |
| US2810651A (en) * | 1954-12-28 | 1957-10-22 | Universal Oil Prod Co | Stabilization of organic compounds |
| US2965685A (en) | 1958-06-24 | 1960-12-20 | Monsanto Chemicals | Polymerization inhibitor |
| NL131752C (enExample) | 1960-09-08 | |||
| US3320305A (en) | 1964-01-28 | 1967-05-16 | Exxon Research Engineering Co | Process for converting nitriles |
| US3696050A (en) | 1970-08-03 | 1972-10-03 | Eastman Kodak Co | Polymerization inhibitors for vinyl monomers and unsaturated polyesters |
| US3704235A (en) | 1971-01-11 | 1972-11-28 | Commissariat Energie Atomique | Stable free radicals of the nitroxide type derived from tropane ring compounds |
| SU763313A1 (ru) * | 1978-10-17 | 1980-09-15 | Волгоградский Политехнический Институт | Способ ингибировани термополимеризации стирола |
| US4202742A (en) | 1979-04-30 | 1980-05-13 | Westinghouse Electric Corp. | Photopolymerization of ethylenically unsaturated monomers |
| US4293347A (en) | 1980-01-21 | 1981-10-06 | The Dow Chemical Company | Process for depolymerization of acrylic acid polymers |
| SU941343A1 (ru) * | 1980-09-26 | 1982-07-07 | Ордена Трудового Красного Знамени Волгоградский Политехнический Институт | Способ предотвращени термополимеризации стирола |
| US4487981A (en) | 1983-09-08 | 1984-12-11 | Atlantic Richfield Company | Inhibiting polymerization of vinyl aromatic monomers |
| JPH0689061B2 (ja) | 1988-12-16 | 1994-11-09 | 日本石油株式会社 | ブタジエン低重合体付加物の製造方法 |
| JP2876331B2 (ja) * | 1990-02-28 | 1999-03-31 | 日本石油化学株式会社 | 付加方法 |
| US5290888A (en) | 1990-07-20 | 1994-03-01 | Ciba-Geigy Corporation | Process for stabilizing ethylenically unsaturated compounds and stabilized monomer compositions |
| US5235056A (en) | 1992-04-22 | 1993-08-10 | Ciba-Geigy Corporation | Substituted 1-hydroxy-2,6-diaryl-4-piperidone ketals and polymer compositions stabilized therewith |
| US5648574A (en) | 1992-10-21 | 1997-07-15 | Betzdearborn Inc. | Compositions and methods for inhibiting vinyl aromatic monomer polymerization |
| US5728872A (en) * | 1994-06-27 | 1998-03-17 | Lutz Riemenschneider | Stabilized acrylic acid compositions |
| US5489720A (en) | 1994-06-30 | 1996-02-06 | Betz Laboratories, Inc. | Methods for inhibiting vinyl aromatic monomer polymerization |
| US5426257A (en) | 1994-06-30 | 1995-06-20 | Betz Laboratories, Inc. | Compositions and methods for inhibiting vinyl aromatic monomer polymerization |
| US5626745A (en) | 1994-10-27 | 1997-05-06 | Water Recycling Systems, Inc. | Waste water purification system |
| US5583247A (en) | 1995-04-14 | 1996-12-10 | Ciba-Geigy Corporation | 7-substituted quinone methides as inhibitors for unsaturated monomers |
| US5648573A (en) | 1995-06-12 | 1997-07-15 | Betzdearborn Inc. | Compositions and methods for inhibiting vinyl aromatic monomer polymerization |
| DE19811602A1 (de) | 1997-03-20 | 1998-11-12 | Ciba Geigy Ag | Polymerisationsinhibitor-Verfahren |
| US5932735A (en) | 1997-06-13 | 1999-08-03 | Ciba Specialty Chemicals Corporation | Derivatives of 1-oxyl-4-hydroxy-2,2,6,6-tetramethylpiperidine as polymerization inhibitors for (meth)acrylate monomers |
| US6020435A (en) | 1997-11-05 | 2000-02-01 | Rohm And Haas Company | Process for preparing polymer core shell type emulsions and polymers formed therefrom |
| US6770222B1 (en) | 1998-03-03 | 2004-08-03 | Nippon Zeon Co., Ltd. | Polymerization-inhibiting composition, polymerization inhibitor and method for inhibiting polymerization |
| TWI224995B (en) | 1998-03-19 | 2004-12-11 | Ciba Sc Holding Ag | Stabilization of wood substrates |
| BR9913523A (pt) | 1998-09-09 | 2001-06-05 | Baker Hughes Inc | Inibição de polimerização de monÈmero estireno utilizando dihidroxiarenos e nitróxidos substituìdos |
| AU5817099A (en) | 1998-09-09 | 2000-03-27 | Baker Hughes Incorporated | Vinyl monomer polymerization inhibition using hindered hydroxylamines |
| US6599326B1 (en) | 1999-01-20 | 2003-07-29 | Ciba Specialty Chemicals Corporation | Inhibition of pulp and paper yellowing using hydroxylamines and other coadditives |
| CA2260310A1 (en) | 1999-01-25 | 2000-07-25 | Rene Dijkstra | Sulfuric acid recovery process and apparatus |
| US6180231B1 (en) | 1999-03-31 | 2001-01-30 | Union Carbide Chemicals & Plastics Technology Corporation | Crosslinkable polyethylene composition |
| EP1065197B1 (en) | 1999-06-28 | 2002-11-06 | Rohm And Haas Company | Process for preparing (meth)acrylic acid |
| AU5917200A (en) * | 1999-08-18 | 2001-03-13 | Nalco/Exxon Energy Chemicals, L.P. | Method of inhibiting vapor phase fouling in vinyl monomer systems |
| DE60023542T2 (de) * | 1999-12-02 | 2006-07-20 | Crompton Corp., Middlebury | Polymerisationsinhibierung von ungesättigten monomeren |
| US6525146B1 (en) | 2000-04-03 | 2003-02-25 | Baker Hughes Incorporated | Inhibition of popcorn polymer growth |
| JP3960508B2 (ja) * | 2000-07-10 | 2007-08-15 | 伯東株式会社 | スチレン類の重合抑制方法 |
| US20030009031A1 (en) | 2001-04-30 | 2003-01-09 | Mikolaj Jawosiuk | Novel hindered spiro-ketal nitroxides |
| WO2003093330A1 (en) * | 2002-05-01 | 2003-11-13 | Ciba Specialty Chemicals Holding Inc. | Process for chain stopping of pvc polymerization |
| EP1587887A1 (en) | 2003-01-29 | 2005-10-26 | Ciba SC Holding AG | Ink-jet ink and recording material |
| CN1901876B (zh) | 2003-10-30 | 2013-04-10 | 西巴特殊化学制品控股公司 | 稳定的身体护理品,家用制品,纺织品和织物 |
| US7282136B2 (en) | 2004-05-26 | 2007-10-16 | Nalco Company | Method of dispersing hydrocarbon foulants in hydrocarbon processing fluids |
| DK1896550T3 (da) | 2005-06-30 | 2013-11-18 | Basf Se | Stabiliserede elektrokrome medier |
| WO2007044396A2 (en) | 2005-10-04 | 2007-04-19 | The Research Foundation Of State University Of New York | Fibronectin polypeptides and methods of use |
| GB0521319D0 (en) | 2005-10-20 | 2005-11-30 | A H Marks And Company Ltd | Method |
| US7985826B2 (en) | 2006-12-22 | 2011-07-26 | Reichhold, Inc. | Molding resins using renewable resource component |
| CA2679066A1 (en) | 2007-02-22 | 2008-08-28 | Othera Holding, Inc. | Hydroxylamine compounds and methods of their use |
| CN103254062A (zh) | 2007-08-31 | 2013-08-21 | 阿科玛股份有限公司 | 在丙烯酸和丙烯酸酯工艺中抑制聚合和结垢的方法 |
| DE102008061611A1 (de) * | 2007-12-19 | 2009-06-25 | Basf Se | Verhinderung der Polymerisation in Wasser-Aromaten-Mischungen |
| US8247593B2 (en) | 2008-05-13 | 2012-08-21 | Nalco Company | Process for preparing substituted 7-cyano quinone methides |
| EP2233505A1 (en) | 2009-03-23 | 2010-09-29 | Total Petrochemicals Research Feluy | Stabilised compositions comprising olefins |
| CN102795966B (zh) | 2011-05-24 | 2014-09-03 | 江苏恒祥化工有限责任公司 | 控制1,4-环己烷二甲醇精馏过程中聚合的方法 |
| US8884038B2 (en) | 2011-06-13 | 2014-11-11 | Nalco Company | Synthesis of 7-acetyleno quinone methide derivatives and their application as vinylic polymerization retarders |
| DE102013204950A1 (de) | 2013-03-20 | 2014-09-25 | Evonik Industries Ag | Verfahren und Zusammensetzung zur Inhibierung der Polymerisation von Cyclopentadienverbindungen |
| US9399622B2 (en) | 2013-12-03 | 2016-07-26 | Ecolab Usa Inc. | Nitroxide hydroxylamine and phenylenediamine combinations as polymerization inhibitors for ethylenically unsaturated monomer processes |
-
2016
- 2016-04-19 BR BR112017022431-3A patent/BR112017022431B1/pt active IP Right Grant
- 2016-04-19 JP JP2017554871A patent/JP6843067B2/ja active Active
- 2016-04-19 CA CA2982465A patent/CA2982465C/en active Active
- 2016-04-19 RU RU2017139281A patent/RU2746125C2/ru active
- 2016-04-19 EP EP16783672.5A patent/EP3289046A4/en not_active Ceased
- 2016-04-19 EP EP25182651.7A patent/EP4628479A2/en active Pending
- 2016-04-19 CN CN201680022901.8A patent/CN107532083A/zh active Pending
- 2016-04-19 KR KR1020177031676A patent/KR102616836B1/ko active Active
- 2016-04-19 US US15/132,844 patent/US10155705B2/en active Active
- 2016-04-19 TW TW105112109A patent/TWI624480B/zh active
- 2016-04-19 WO PCT/US2016/028239 patent/WO2016172076A1/en not_active Ceased
- 2016-04-20 AR ARP160101084A patent/AR104327A1/es active IP Right Grant
-
2017
- 2017-10-15 SA SA517390157A patent/SA517390157B1/ar unknown
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5221498A (en) * | 1991-07-22 | 1993-06-22 | Betz Laboratories, Inc. | Methods and compositions for inhibitoring polymerization of vinyl monomers |
| WO2001040404A1 (en) * | 1999-12-03 | 2001-06-07 | Uniroyal Chemical Company, Inc. | Composition and method for inhibiting polymerization and polymer growth |
| WO2006078123A1 (en) * | 2005-01-18 | 2006-07-27 | Yeochun Ncc Co., Ltd. | Polymerization inhibitor for 1,3-butadiene and a method of inhibiting polymerization of 1,3-butadiene by imputing thereof |
Non-Patent Citations (1)
| Title |
|---|
| See also references of EP3289046A4 * |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11180578B2 (en) | 2018-07-13 | 2021-11-23 | Ecolab Usa Inc. | Polymerization inhibitor and retarder compositions with amine stabilizer |
| EP3763779A1 (en) | 2019-07-09 | 2021-01-13 | SK Innovation Co., Ltd. | Lubricant composition and method of preparing copolymer using the same |
| KR20210006634A (ko) | 2019-07-09 | 2021-01-19 | 에스케이이노베이션 주식회사 | 윤활 조성물 및 이를 이용한 공중합체의 제조 방법 |
| US11118129B2 (en) | 2019-07-09 | 2021-09-14 | Sk Innovation Co., Ltd. | Lubricant composition and method of preparing copolymer using the same |
| KR102803771B1 (ko) | 2019-07-09 | 2025-05-02 | 에스케이이노베이션 주식회사 | 윤활 조성물 및 이를 이용한 공중합체의 제조 방법 |
| US11396629B2 (en) | 2019-10-11 | 2022-07-26 | Ecolab Usa Inc. | Quinone methide and ammonium salt antipolymerant composition and method |
| EP3868792A1 (en) | 2020-02-20 | 2021-08-25 | SK Innovation Co., Ltd. | Method of producing ethylene-carboxylic acid compolymer |
| KR20210106092A (ko) | 2020-02-20 | 2021-08-30 | 에스케이이노베이션 주식회사 | 에틸렌-카르복실산 공중합체의 제조 방법 |
| US11685795B2 (en) | 2020-02-20 | 2023-06-27 | Sk Innovation Co., Ltd. | Method of producing ethylene-carboxylic acid compolymer |
Also Published As
| Publication number | Publication date |
|---|---|
| CA2982465C (en) | 2024-05-14 |
| JP6843067B2 (ja) | 2021-03-17 |
| SA517390157B1 (ar) | 2022-05-16 |
| EP4628479A2 (en) | 2025-10-08 |
| TWI624480B (zh) | 2018-05-21 |
| EP3289046A4 (en) | 2018-12-12 |
| BR112017022431A2 (pt) | 2018-07-10 |
| KR20170138455A (ko) | 2017-12-15 |
| CN107532083A (zh) | 2018-01-02 |
| TW201700502A (zh) | 2017-01-01 |
| EP3289046A1 (en) | 2018-03-07 |
| AR104327A1 (es) | 2017-07-12 |
| JP2018513258A (ja) | 2018-05-24 |
| BR112017022431B1 (pt) | 2023-03-28 |
| RU2017139281A3 (enExample) | 2019-08-28 |
| US10155705B2 (en) | 2018-12-18 |
| RU2746125C2 (ru) | 2021-04-07 |
| US20160304417A1 (en) | 2016-10-20 |
| CA2982465A1 (en) | 2016-10-27 |
| RU2017139281A (ru) | 2019-05-21 |
| KR102616836B1 (ko) | 2023-12-20 |
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