TW588057B - Method for shortstopping polymerization processes in the manufacture of synthetic rubbers - Google Patents

Method for shortstopping polymerization processes in the manufacture of synthetic rubbers Download PDF

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TW588057B
TW588057B TW90127176A TW90127176A TW588057B TW 588057 B TW588057 B TW 588057B TW 90127176 A TW90127176 A TW 90127176A TW 90127176 A TW90127176 A TW 90127176A TW 588057 B TW588057 B TW 588057B
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parts
weight
polymerization
hydroxylamine
mixture
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TW90127176A
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Chinese (zh)
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Hartmut K Stiller
Hans A R Edel
Doris R Marx
Heinz-Jurgen Bogen
Ilona Guth
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Dow Global Technologies Inc
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F293/00Macromolecular compounds obtained by polymerisation on to a macromolecule having groups capable of inducing the formation of new polymer chains bound exclusively at one or both ends of the starting macromolecule
    • C08F293/005Macromolecular compounds obtained by polymerisation on to a macromolecule having groups capable of inducing the formation of new polymer chains bound exclusively at one or both ends of the starting macromolecule using free radical "living" or "controlled" polymerisation, e.g. using a complexing agent

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polymerisation Methods In General (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

This invention is related to a new shortstopping combination for use in stopping free radical and redox initiated polymerization is the combination of hydroxylamine (free base) (HA) and i-propylhydroxylamine (IPAH). It is more effective as related N-alcylated-hydroxylamines with regard to mooney stability. The combination is not corrosive to metals used in commercial equipment for emulsion polymerization and prevents the rust formation and the formation of nitrosamines, coagulate and precipitate.

Description

588057 五、發明説明(1 ) 本發明係有關一種製造合成橡膠(諸如丁二烯·苯乙埽 共聚物)時,速止聚合作用過程的改進方法。 由自由基或氧化還原所啟始的乳膠聚合作用通常係藉 由混合乳膠和速止劑來終止,其係用以預防自由基或氧^ 還原反應繼續進行。該聚合作用必須終止以獲得具有所欲 特性之產物。所生產之聚合物之特性依其單體轉換率 同。 自由基或氧化還原聚合作用主要應用在製造彈性物質 的乳膠聚合反應,諸如苯乙烯-丁二烯橡膠(sbr),丁二烯 橡膠(BR),和丙烯腈·丁二烯橡膠(NBR)。 許多研究希望能找到良好的速止劑,同時已發現許多 有用的化合物。然而現在使用的化合物有某些缺點且一般 係不適用於所有的聚合作用系統,一些習知的傳統速止劑 如胺基甲酸酯、氫醌、氫辛(hydracine)、多硫化物、硝化 合物、N·脂環化羥胺和/或其它(us 5.348 372 us 3.296.m; EP 656 371; EP-AO 437 293; DE-A-15 95 177)等。 N-單丁羥胺被建議用作速止劑,特別是異丙羥胺 (IPHA)(在 US 5.384.372; WO 98/51714)。在本例中,最終 橡膠中並無亞硝基胺和其前驅物存在。 所述方法的缺點是此非一完全速止過程,因其有門尼 黏度之飄移且在回收槽内形成凝集物及沉澱物。另一個問 題是當使用N,N-二脂環化羥胺和/或胺基甲酸酯時會形成 二級胺。 此問題已經由使用羥胺(HA)(游離鹼)和異丙經胺之混 本紙張尺度適用中國國家標準(CNS) A4規格(210X297公釐) 588057 A7 ____B7 _ 五、發明^~ ' 合物作為速止劑而解決。在此方式,可製成沒有凝集物和 沉澱物的乳膠,以及沒有亞硝基胺和其前驅物的橡膠。乳 膠或橡膠中亦不會發現門尼黏度的飄移。 本發明係有關一種用於終止由自由基所啟始之乳化聚 合作用的方法,其包含加入一由異丙羥胺(IpAH)和羥胺 (HA)(游離鹼)混合物所組成的速止劑。 根據本發明顯示一製備合成橡膠過程,其在水性媒質 中由自由基和氧化還原反應引起之共軛雙烯和單烯烴之橡 膠聚合作用,經由加入由羥胺(游離鹼)(HA)和異丙羥胺 (IPAH)所構成的速止劑來中和聚合反應。 此過程特徵在於由羥胺(游離鹼)(HA)和異丙羥胺 (IPAH)所構成的混合物作為速止劑,其包含: a) 依每100份之初始饋入之單體計為〇 〇〇1到〇 499重 量份的HA, b) 依每100份之初始饋入之單體計為〇 499到〇 〇〇1重 量份的IPHA。 較佳地,加入一由0.01到0.2重量份的HA和0.2到0.01 重量份的IPAH所構成之混合物。 該混合之速止劑係依每1 〇〇重量份之初始單體(phm)的 0.005到0.2重量份的量來加入,且較佳為初始單體(phm)的 0.1到0.4重量份。 此速止劑添加的方式是以橡膠聚合方法的傳統技術來 發生,較佳地,當獲得預期轉換時將原始溶液(50% HA, 15% IPHA)及/或是速止劑混合物之水溶液加入聚合反應 本紙張尺度適用中國國家標準(CNS) A4規格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁)588057 V. Description of the invention (1) The present invention relates to an improved method for quick-stop polymerization when manufacturing synthetic rubber (such as a butadiene-styrene-acrylidine copolymer). Latex polymerization initiated by free radicals or redox is usually terminated by mixing latex and shortstop, which is used to prevent free radical or oxygen reduction reaction from continuing. The polymerization must be terminated to obtain a product having the desired characteristics. The properties of the produced polymer are the same according to its monomer conversion rate. Free radical or redox polymerization is mainly used in latex polymerization to make elastic materials, such as styrene-butadiene rubber (sbr), butadiene rubber (BR), and acrylonitrile-butadiene rubber (NBR). Many studies hope to find good shortstops, and many useful compounds have been found. However, the compounds currently used have certain disadvantages and are generally not suitable for all polymerization systems. Some conventional traditional short-stop agents such as carbamate, hydroquinone, hydracine, polysulfide, nitrate Compounds, N · alicyclic hydroxylamine and / or others (us 5.348 372 us 3.296.m; EP 656 371; EP-AO 437 293; DE-A-15 95 177) and the like. N-monobutylhydroxylamine is suggested as a shortstop, especially isopropylhydroxylamine (IPHA) (in US 5.384.372; WO 98/51714). In this example, no nitrosoamine and its precursors were present in the final rubber. The disadvantage of this method is that this process is not a complete quick stop because it has a drift in Mooney viscosity and forms agglomerates and precipitates in the recovery tank. Another problem is the formation of secondary amines when N, N-dialicyclic hydroxylamines and / or carbamates are used. This problem has been caused by the use of hydroxylamine (HA) (free base) and isopropyl amine mixed paper size applicable to Chinese National Standard (CNS) A4 specifications (210X297 mm) 588057 A7 ____B7 _ V. Invention ^ ~ 'Compound as Quick stop agent. In this way, latexes without agglutinates and precipitates, and rubbers without nitrosoamines and their precursors can be made. No shift in Mooney viscosity was found in latex or rubber. The present invention relates to a method for stopping emulsification polymerization initiated by free radicals, which comprises adding a short-stop agent composed of a mixture of isopropylhydroxylamine (IpAH) and hydroxylamine (HA) (free base). According to the present invention, a process for preparing a synthetic rubber is shown. In an aqueous medium, the rubber polymerization of conjugated diene and monoolefin caused by free radicals and redox reactions is performed by adding hydroxylamine (free base) (HA) and isopropyl A shortstop composed of hydroxylamine (IPAH) to neutralize the polymerization reaction. This process is characterized by a mixture of hydroxylamine (free base) (HA) and isopropylhydroxylamine (IPAH) as the short-stop agent, which contains: a) Calculated based on 100 parts of the initial fed monomer as 0.00 1 to 0499 parts by weight of HA, b) 0499 to 001 parts by weight of IPHA per 100 parts of the initially fed monomer. Preferably, a mixture consisting of 0.01 to 0.2 parts by weight of HA and 0.2 to 0.01 parts by weight of IPAH is added. The mixed shortstop is added in an amount of 0.005 to 0.2 parts by weight per 100 parts by weight of the initial monomer (phm), and preferably 0.1 to 0.4 parts by weight of the initial monomer (phm). This shortstop is added using the traditional technique of rubber polymerization. Preferably, the original solution (50% HA, 15% IPHA) and / or an aqueous solution of the shortstop mixture is added when the desired conversion is obtained. Polymerization This paper is sized for China National Standard (CNS) A4 (210X297 mm)

588057 五、發明説明(3 ) 中。 所使用之聚合系統係較佳為苯乙烯丁二烯聚合作用。 本發明的實用性藉由增加下列例子進一步説明,其僅 供用於例示而非本發明的限制範圍。下列例子中之名詞,, 份”是指每100份之饋入單體中的速止劑重量份。 實施例 表一中,我們以使用c〇uld皂苯乙婦丁二烯聚合作用來 進行自由基或氧化還原所啟始之橡膠聚合作用: 表一 水 脂肪酸皂 所有聚合作用在5°c下進行,以達至約60%的單體聚合 物轉換率。 〇 接著加入速止劑。 範例1以90/1 〇重量比例的二甲基二硫基胺甲酸酯 本紙張尺度適用中國國家標準(CNS) Α4規格(21〇><297公爱)588057 V. Description of the invention (3). The polymerization system used is preferably styrene butadiene polymerization. The practicality of the present invention is further illustrated by adding the following examples, which are provided for illustration only and are not intended to limit the scope of the present invention. The term "parts" in the following examples refers to parts by weight of the short-stopper per 100 parts of the monomer fed into the monomer. In Table 1 of the Examples, we performed the polymerization using could soap styrene ethyl butadiene Free radical or redox-initiated rubber polymerization: Table 1 All polymerization of water fatty acid soap is performed at 5 ° C to achieve a monomer polymer conversion rate of about 60%. 〇Then add a shortstop. Example 1 Dimethyldithiocarbamate in a weight ratio of 90/1 〇 This paper size is applicable to China National Standard (CNS) A4 specifications (21〇 < 297 public love)

..... ............... (請先閲讀背面之注意事項再填寫本頁) 、可丨 588057 發明説明(4 (dtc)和二乙基羥胺(DEHA)混合稀釋水溶液進行速止。 範例2, 3,4, 5, 6, 7,和8以50%的羥胺(HA)和15%的異 (請先閲讀背面之注意事項再填寫本頁) 丙羥胺(IPAH)混合成22%的水溶液進行速止反應,結果列 在表二。 此二種化合物的混合物被形成批料或是線上添加,原 始化合物加入或是沒有加入去離子水。活性化合物在水中 的較佳濃度分別從1%到25%不等。 當達到預期之聚合程度時,將速止劑直接加入乳膠中。 亞硝基胺的存在是使用BGA方法,以熱能分析儀,氣 相分析法來測定。 表二 範例 DTC/D EHA (phm) HA (phm) IPAH (phm) 亞硝基 胺* (ppb) 門尼 凝集物/ 沉澱物 (%phr) 速止後 之乳膠 單體回 收後之 乳膠 1 0.2 - 麵 12.7*1 48 52 4.5 2 - 0.1 0.1 n.d.*3 48 48 0 3 - 0.01 0.19 n.d. 48 49 0 4 - 0.08 0.12 n.d. 48 48 0 5 - 0.19 0.01 n.d. 48 47 0 6 - 0.02 0.02 n.d. 48 48 0 7 - 0.001 0.449 n.d. 48 48 0 8 - 0.449 0.001 n.d. 48 48 0 *偵測:N-亞硝基二甲胺,N-亞硝基二乙胺,N-亞硝基二 丙胺,N-亞硝基二丁胺,N_亞硝基哌啶,N-亞硝基吡咯烷5 N-亞硝基嗎啉 *1)橡膠中的N-亞硝基二甲胺和N-亞硝基二乙胺的概述 本紙張尺度適用中國國家標準(CNS) A4規格(210X297公釐) 588057 五、發明説明(5 ) *2)單體回收之後偵測凝集物/沉澱物 *3)偵測不到 將50%的羥胺(游離鹼)(hA)和i 5%的異丙羥胺水溶液 加入原始溶液進行速止反應。 範例1使用傳統速止劑,其結果橡膠中偵測到高含量的 亞石肖基胺’同時發現高量的二甲基二硫基胺甲酸酯(DTC) 和N,N-二乙基羥胺(DEHA)凝集物(範例丨)。 令人驚訝地,使用羥胺(HA)異丙羥胺(1]?人11)的結果測 不到亞硝基胺和凝集,同時產生一非常穩定不會飄移的乳 膠(範例2-8)。 本發明的優點是此為一較佳的速止方法,同時對於在 氣相及液相-(乳膠)驟成之塊狀有較佳之防止作用。此外, 該二種混合形成速止劑之化合物所需的量較任一使用單一 化合物的量為少,表示此二化合物在進行速止反應時有協 乘效果存在。 本紙張尺度適用中國國家標準(CNs) A4規格(210X297公釐)..... ......... (Please read the notes on the back before filling out this page), Ke 588057 Description of Invention (4 (dtc), and diethylhydroxylamine ( DEHA) Mix the diluted aqueous solution for quick stop. Examples 2, 3, 4, 5, 6, 7, and 8 use 50% hydroxylamine (HA) and 15% isopropyl (Please read the precautions on the back before filling this page) Propanolamine (IPAH) was mixed into a 22% aqueous solution for quick-stop reaction, and the results are shown in Table 2. The mixture of these two compounds was formed into batches or added online, with or without the original compound and deionized water. Active compounds The preferred concentration in water ranges from 1% to 25%. When the desired degree of polymerization is reached, the shortstop is added directly to the latex. The presence of nitrosoamine is the BGA method, using a thermal energy analyzer, gas Phase analysis method. Table 2 Example DTC / D EHA (phm) HA (phm) IPAH (phm) Nitrosamine * (ppb) Mooney agglomerates / precipitates (% phr) Latex monomers short-stopped Latex recovered 1 0.2-12.7 * 1 48 52 4.5 2-0.1 0.1 nd * 3 48 48 0 3-0.01 0.19 nd 48 49 0 4-0.08 0.12 nd 48 48 0 5-0 .19 0.01 nd 48 47 0 6-0.02 0.02 nd 48 48 0 7-0.001 0.449 nd 48 48 0 8-0.449 0.001 nd 48 48 0 * Detection: N-nitrosodimethylamine, N-nitrosodiamine Ethylamine, N-nitrosodipropylamine, N-nitrosodibutylamine, N-nitrosopiperidine, N-nitrosopyrrolidine 5 N-nitrosomorpholine * 1) N in rubber -Overview of Nitrosodimethylamine and N-Nitrosodiethylamine This paper size applies Chinese National Standard (CNS) A4 (210X297 mm) 588057 5. Description of the invention (5) * 2) After monomer recovery Detect agglutinates / precipitates * 3) Undetectable Add 50% hydroxylamine (free base) (hA) and i 5% isopropylhydroxylamine aqueous solution to the original solution for quick stop reaction. Example 1 The use of a conventional short-stop agent. As a result, a high content of schistolidamine was detected in the rubber, and a high amount of dimethyldithiocarbamate (DTC) and N, N-diethylhydroxylamine ( DEHA) agglutinate (example 丨). Surprisingly, the results of using hydroxylamine (HA), isopropylhydroxylamine (1), and human 11) did not detect nitrosoamine and agglutination, while producing a very stable latex that did not drift (Examples 2-8). The advantage of the present invention is that this is a better quick-stop method, and at the same time, it has a better prevention effect on the block formed in the gas phase and the liquid phase (latex). In addition, the amount of the two compounds that are used to form a short-stop agent is less than the amount of any single compound, indicating that the two compounds have a synergistic effect when the short-stop reaction is performed. This paper size applies to Chinese National Standards (CNs) A4 (210X297 mm)

、?r— (請先閲讀背面之注意事項再填寫本頁),? R— (Please read the notes on the back before filling this page)

Claims (1)

申請專利範圍修正本 六、申請專利範圍 第090127176號專利申請案 修正日期:92年7月 1· 一種速止自由基或氧脊、萝店&人 _ X虱化還原聚合作用的方法,其包 a種由|工月女(ΗΑ)和異丙經胺(ΙρΑΗ)所組成的混 δ物加入達到預期轉換率的聚合混合物中。 2. 如申請專利範圍第卜員之方法,其中該混合物係以 每100份初始單體重量份(Phm)為0.005到〇.2重量份 的量被加入。 3. 如申請專利範圍第β之方法,其中該混合物由依 初始單體(phm)計為〇·〇〇ι到〇 499重量份的羥胺(ΗΑ) 和0.499到0.001重量份的異丙羥胺(ΙρΑΗ)κ組成。 4·如申請專利範圍第3項之方法,其中該混合物由依 初始單體(phm)計為〇·〇 1到〇·2重量份的羥胺(ΗΑ)和 0.2到0.1重量份的異丙羥胺(ΙΡαη)所組成。 5· 如申請專利範圍第1項之方法,其中該等速止劑係 以下列二種成份的原始濃度被使用,即為15%配於 水中之ΙΡΑΗ和50%配於水中之ΗΑ。Application for amendment of patent scope VI. Application for patent scope No. 090127176 Patent application amendment date: July 1992 1. A method of quick-stop free radical or oxygen spine, Luodian & human_ X lice reduction reduction polymerization, which A type of mixed δ composed of a worker month (ΗΑ) and isopropylamine (ΙρΑΗ) was added to the polymerization mixture to achieve the expected conversion rate. 2. The method as claimed in the patent application scope, wherein the mixture is added in an amount of 0.005 to 0.2 parts by weight per 100 parts by weight of the initial monomer (Phm). 3. The method as claimed in claim No. β, wherein the mixture is from 0.0000 to 0499 parts by weight of hydroxylamine (VIIA) and 0.499 to 0.001 parts by weight of isopropylhydroxylamine (ΙρΑΗ) based on the initial monomer (phm). ) κ composition. 4. The method according to item 3 of the patent application, wherein the mixture is composed of 0.001 to 0.2 parts by weight of hydroxylamine (VIIA) and 0.2 to 0.1 parts by weight of isopropyl hydroxylamine (based on the initial monomer (phm) IPαη). 5. As in the method of applying for item 1 of the patent scope, the short-stop agents are used at the original concentrations of the following two ingredients, namely 15% IPAΗ in water and 50% ΗΑ in water.
TW90127176A 2000-11-07 2001-11-01 Method for shortstopping polymerization processes in the manufacture of synthetic rubbers TW588057B (en)

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JP5658169B2 (en) * 2009-01-14 2015-01-21 スティロン ヨーロッパ ゲゼルシャフト ミット ベシュレンクテル ハフツング Method for increasing monomer conversion in emulsion polymerization.
BR112014030662B1 (en) 2012-06-14 2021-07-06 Dow Global Technologies Llc method for terminating a free radical initiated emulsion polymerization reaction and method for producing an elastomer
US9309331B2 (en) 2012-09-28 2016-04-12 Angus Chemical Company Alkyl hydroxylamine compounds and their use for shortstopping free radical polymerizations

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US3296177A (en) * 1964-11-13 1967-01-03 Pennsalt Chemicals Corp Stopping agents for synthetic rubber polymerization
US4912239A (en) * 1987-11-13 1990-03-27 Dow Corning Corporation Method for stabilizing unsaturated organosilicone compositions
CA2099168A1 (en) * 1992-10-21 1994-04-22 Betzdearborn Inc. Compositions and methods for inhibiting styrene polymerization
IT1265250B1 (en) * 1993-12-03 1996-10-31 Enichem Elastomers PROCEDURE FOR THE TERMINATION OF EMULSION CURING THAT DOES NOT GENERATE NITROSAMINES
US5384372A (en) * 1994-03-30 1995-01-24 The Goodyear Tire & Rubber Company Shortstopping of free radical polymerizations
WO1998051714A1 (en) * 1997-05-16 1998-11-19 Angus Chemical Company N-ethylhydroxylamine as a shortstopping agent for free radical polymerization
US6495065B1 (en) * 1999-09-09 2002-12-17 Atofina Chemicals, Inc. Nitrosamine-inhibiting compositions for shortstopping of free radical emulsion polymerizations

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