CN118546279A - New decanoic acid rare earth catalyst for polymerization and preparation method and application thereof - Google Patents
New decanoic acid rare earth catalyst for polymerization and preparation method and application thereof Download PDFInfo
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Abstract
本发明涉及催化剂技术领域,具体涉及一种聚合用新癸酸稀土催化剂及其制备方法与应用,所述新癸酸稀土催化剂包括如下组分:新癸酸钕、含卤素化合物、醇类化合物、共轭二烯烃和助剂,所述助剂包括三苯基(甲基)‑四(五氟苯)硼酸盐和苯基‑二甲基氨基‑四苯基硼酸盐的混合物,两者摩尔比2‑4:1,本发明的稀土催化剂制备得到的聚丁二烯产品顺式结构含量、分子量和收率较高,同时分子量分布较窄,原料易得,成本较低。The invention relates to the technical field of catalysts, and in particular to a neodecanoic acid rare earth catalyst for polymerization, a preparation method and an application thereof. The neodecanoic acid rare earth catalyst comprises the following components: neodymium neodecanoate, a halogen-containing compound, an alcohol compound, a conjugated diene and an auxiliary agent, wherein the auxiliary agent comprises a mixture of triphenyl(methyl)-tetrakis(pentafluorobenzene)borate and phenyl-dimethylamino-tetraphenylborate, and the molar ratio of the two is 2-4:1. The polybutadiene product prepared by the rare earth catalyst has high cis-structure content, molecular weight and yield, and has a narrow molecular weight distribution, and the raw materials are easily available and the cost is low.
Description
技术领域Technical Field
本发明涉及催化剂技术领域,具体涉及一种聚合用新癸酸稀土催化剂及其制备方法与应用。The invention relates to the technical field of catalysts, and in particular to a neodecanoic acid rare earth catalyst for polymerization and a preparation method and application thereof.
背景技术Background Art
顺丁橡胶是顺式-1,4-聚丁二烯橡胶的简称,其分子式为(C4H6)n。顺丁橡胶是由1,3-丁二烯聚合而成的结构规整的合成橡胶,其顺式结构含量在95%以上。顺丁橡胶特别适用于制造汽车轮胎和耐寒制品,还可以制造缓冲材料及各种胶鞋、胶布、胶带和海绵胶等。Butadiene rubber is the abbreviation of cis-1,4-polybutadiene rubber, and its molecular formula is (C 4 H 6 ) n . Butadiene rubber is a synthetic rubber with a regular structure formed by the polymerization of 1,3-butadiene, and its cis structure content is more than 95%. Butadiene rubber is particularly suitable for manufacturing automobile tires and cold-resistant products, and can also be used to manufacture cushioning materials and various rubber shoes, rubber cloths, tapes and sponge rubbers.
1,3-丁二烯为单体制备顺丁橡胶的聚合反应是一种高度立体定向的反应,可提供各种具有不同微观结构的聚丁二烯,并影响橡胶的基本性质。1,3-丁二烯的立体选择性主要由调整聚合参数(即反应温度、使用的溶剂和催化剂系统)来控制。顺丁橡胶根据催化剂的不同,可分成镍系、钴系、钛系和稀土系(钕系)顺丁橡胶。The polymerization reaction of 1,3-butadiene as a monomer to prepare butadiene rubber is a highly stereospecific reaction that can provide a variety of polybutadiene with different microstructures and affect the basic properties of rubber. The stereoselectivity of 1,3-butadiene is mainly controlled by adjusting the polymerization parameters (i.e., reaction temperature, solvent used, and catalyst system). Butadiene rubber can be divided into nickel-based, cobalt-based, titanium-based, and rare earth (neodymium-based) butadiene rubber according to the different catalysts.
稀土催化剂一般是以稀土化合物为主催化剂的多组分体系。当主催化剂为含有卤素的稀土化合物时,通常加入烷基铝即可形成具有催化活性的催化剂,是为二元体系。当主催化剂为不含卤素的稀土化合物时,除了加入烷基铝,还必须加入可提供卤素的路易斯酸,才可以形成具有催化活性的催化剂,是为三元体系。此外,为了提高催化剂的活性、改善催化剂相态、调节聚合的分子量和微观结构,通常还需要加入一些调节剂,如二烯烃、羧酸以及芳香烃等。Rare earth catalysts are generally multi-component systems with rare earth compounds as the main catalyst. When the main catalyst is a rare earth compound containing halogen, alkyl aluminum is usually added to form a catalyst with catalytic activity, which is a binary system. When the main catalyst is a rare earth compound without halogen, in addition to adding alkyl aluminum, a Lewis acid that can provide halogen must also be added to form a catalyst with catalytic activity, which is a ternary system. In addition, in order to improve the activity of the catalyst, improve the catalyst phase, and adjust the molecular weight and microstructure of the polymerization, it is usually necessary to add some regulators, such as dienes, carboxylic acids, and aromatic hydrocarbons.
然而现阶段的稀土催化体系催化剂存在制备过程繁琐、组成复杂、成本较高的问题,聚丁二烯橡胶产品产率低,且大部分稀土催化体系尚未实现高于98%1,4-顺式选择性,导致其实际应用受限。However, the current rare earth catalytic system catalysts have the problems of cumbersome preparation process, complex composition and high cost. The yield of polybutadiene rubber products is low, and most rare earth catalytic systems have not yet achieved a 1,4-cis selectivity higher than 98%, which limits their practical application.
比如中国专利申请CN113929802A公开了一种新癸酸稀土催化剂及其制备方法和应用,该稀土催化剂包括:a、磷酸钕化合物;b、共轭二烯烃;c、烷基铝或氢化烷基铝,或二者的混合物;d、含卤素化合物;其中,各组分摩尔比为a:b:c:d=1:(2~50):(5~40):(1~20)。该发明提供的稀土催化剂制备得到的聚丁二烯橡胶产品顺式结构含量在98%以下、分子量分布Mw/Mn在2以上,因此,顺式结构含量有待进一步提高,分子量分布有待进一步缩窄。For example, Chinese patent application CN113929802A discloses a neodecanoic acid rare earth catalyst and its preparation method and application, the rare earth catalyst comprising: a, neodymium phosphate compound; b, conjugated diene; c, alkyl aluminum or alkyl aluminum hydride, or a mixture of the two; d, halogen-containing compound; wherein the molar ratio of each component is a:b:c:d=1:(2-50):(5-40):(1-20). The polybutadiene rubber product prepared by the rare earth catalyst provided by the invention has a cis structure content of less than 98% and a molecular weight distribution Mw/Mn of more than 2. Therefore, the cis structure content needs to be further increased and the molecular weight distribution needs to be further narrowed.
中国专利CN117264103B公开了一种含有新癸酸钕的稀土催化剂及基于该催化剂的聚丁二烯橡胶的制备方法。所述含有新癸酸钕的稀土催化剂由新癸酸钕、醇类化合物、甲基铝氧烷、共轭二烯烃和离子液体制成。该发明提供的稀土催化剂具有高活性、高顺式选择性优点,可制备得到兼具超高顺式、高分子量、窄分子量分布等特点的高品质聚丁二烯橡胶产品,且该产品收率高。但是该催化剂中采用了离子液体,制备过程复杂,且成本较高。Chinese patent CN117264103B discloses a rare earth catalyst containing neodymium neodecanoate and a method for preparing polybutadiene rubber based on the catalyst. The rare earth catalyst containing neodymium neodecanoate is made of neodymium neodecanoate, alcohol compounds, methylaluminoxane, conjugated dienes and ionic liquids. The rare earth catalyst provided by the invention has the advantages of high activity and high cis selectivity, and can prepare high-quality polybutadiene rubber products with the characteristics of ultra-high cis, high molecular weight, narrow molecular weight distribution, etc., and the product has a high yield. However, ionic liquids are used in the catalyst, the preparation process is complicated, and the cost is relatively high.
因此,开发一种能解决上述技术问题的新癸酸稀土催化剂及其制备方法和应用是非常必要的。Therefore, it is very necessary to develop a neodecanoic acid rare earth catalyst and a preparation method and application thereof that can solve the above-mentioned technical problems.
发明内容Summary of the invention
本发明的目的是克服现有技术的不足而提供一种新癸酸稀土催化剂及其制备方法和应用,本发明的新癸酸稀土催化剂制备得到的聚丁二烯产品顺式结构含量、分子量和收率较高,同时分子量分布较窄,原料易得,成本较低。The purpose of the present invention is to overcome the deficiencies of the prior art and provide a neodecanoic acid rare earth catalyst and a preparation method and application thereof. The polybutadiene product prepared by the neodecanoic acid rare earth catalyst of the present invention has a high cis structure content, molecular weight and yield, and a narrow molecular weight distribution. The raw materials are easily available and the cost is low.
本发明是通过以下技术方案予以实现的:The present invention is achieved through the following technical solutions:
一种聚合用新癸酸稀土催化剂,包括如下组分:新癸酸钕、含卤素化合物、醇类化合物、共轭二烯烃和助剂,所述助剂包括三苯基(甲基)-四(五氟苯)硼酸盐和苯基-二甲基氨基-四苯基硼酸盐的混合物,两者摩尔比2-4:1。A rare earth neodecanoate catalyst for polymerization comprises the following components: neodymium neodecanoate, a halogen-containing compound, an alcohol compound, a conjugated diene and an auxiliary agent, wherein the auxiliary agent comprises a mixture of triphenyl(methyl)-tetrakis(pentafluorobenzene)borate and phenyl-dimethylamino-tetraphenylborate, with a molar ratio of 2-4:1.
优选地,所述含卤素化合物包括烷基卤化铝。Preferably, the halogen-containing compound comprises an alkylaluminum halide.
更优选地,所述烷基卤化铝包括一氯二乙基铝和三氯二异丁基铝中的至少一种。More preferably, the alkylaluminum halide includes at least one of diethylaluminum monochloride and diisobutylaluminum trichloride.
更优选地,所述烷基卤化铝为一氯二乙基铝和三氯二异丁基铝的混合物,两者摩尔比1-3:1。More preferably, the alkyl aluminum halide is a mixture of diethylaluminum monochloride and diisobutylaluminum trichloride, with a molar ratio of 1-3:1.
优选地,所述醇类化合物包括异丙醇和环己醇中的至少一种。Preferably, the alcohol compound includes at least one of isopropanol and cyclohexanol.
更优选地,所述醇类化合物为异丙醇和环己醇的混合物,两者摩尔比3-5:1。More preferably, the alcohol compound is a mixture of isopropanol and cyclohexanol, with a molar ratio of 3-5:1.
优选地,所述共轭二烯烃为异戊二烯和/或间戊二烯。Preferably, the conjugated diene is isoprene and/or piperylene.
优选地,新癸酸钕中的钕元素、含卤素化合物、醇类化合物、共轭二烯烃、助剂的摩尔比为1:1-20:5-10:20-80:1-5。Preferably, the molar ratio of the neodymium element, the halogen-containing compound, the alcohol compound, the conjugated diene, and the additive in the neodymium neodecanoate is 1:1-20:5-10:20-80:1-5.
更优选地,新癸酸钕中的钕元素、含卤素化合物、醇类化合物、共轭二烯烃、助剂的摩尔比为1:5-15:6-8:30-70:2-4。More preferably, the molar ratio of the neodymium element, the halogen-containing compound, the alcohol compound, the conjugated diene, and the additive in the neodymium neodecanoate is 1:5-15:6-8:30-70:2-4.
优选地,所述新癸酸钕的制备方法包括如下步骤:Preferably, the method for preparing neodymium neodecanoate comprises the following steps:
(1)将氧化钕用盐酸溶解,控制pH为4.5-5.0,除杂质得到氯化钕NdCl3溶液;(1) dissolving neodymium oxide with hydrochloric acid, controlling the pH to 4.5-5.0, and removing impurities to obtain a neodymium chloride NdCl3 solution;
(2)将步骤(1)的NdCl3溶液静置,过滤沉淀,得到澄清的NdCl3溶液;(2) allowing the NdCl3 solution of step (1) to stand, filtering and precipitating to obtain a clarified NdCl3 solution;
(3)将新癸酸和正己烷混合,加入浓度为5mol/L的氢氧化钠溶液,在60-65℃下进行皂化反应30-35分钟得到反应液;(3) mixing neodecanoic acid and n-hexane, adding a 5 mol/L sodium hydroxide solution, and performing a saponification reaction at 60-65° C. for 30-35 minutes to obtain a reaction solution;
(4)将澄清的NdCl3溶液加入步骤(3)的反应液中,混合反应20分钟以上,静置分相;(4) adding the clarified NdCl3 solution to the reaction solution of step (3), mixing and reacting for more than 20 minutes, and standing to separate the phases;
(5)将步骤(4)上层成品进一步过滤,除杂质完成即得。(5) The upper layer of the finished product in step (4) is further filtered to remove impurities.
更优选地,所述氧化钕的用量为23-24重量份,新癸酸170-178重量份,正己烷185-195重量份,氢氧化钠溶液50-55重量份。More preferably, the amount of neodymium oxide is 23-24 parts by weight, neodecanoic acid is 170-178 parts by weight, n-hexane is 185-195 parts by weight, and sodium hydroxide solution is 50-55 parts by weight.
本发明还涉及上述的新癸酸稀土催化剂的制备方法,包括如下步骤:The present invention also relates to a method for preparing the above-mentioned neodecanoic acid rare earth catalyst, comprising the following steps:
1)在惰性气氛下,将新癸酸钕、醇类化合物、助剂和共轭二烯烃溶于有机溶剂中,得到混合溶液A;1) Under an inert atmosphere, dissolving neodymium neodecanoate, an alcohol compound, an auxiliary agent and a conjugated diene in an organic solvent to obtain a mixed solution A;
2)在混合溶液A中加入含卤素化合物,得到混合溶液B,陈化15-30min即得。2) Add a halogen-containing compound to the mixed solution A to obtain a mixed solution B, and age it for 15-30 minutes.
优选地,步骤1)中所述有机溶剂为惰性有机溶剂。Preferably, the organic solvent in step 1) is an inert organic solvent.
更优选地,所述惰性有机溶剂包括饱和脂肪烃和/或脂环烃。More preferably, the inert organic solvent comprises saturated aliphatic hydrocarbons and/or alicyclic hydrocarbons.
更优选地,所述惰性有机溶剂包括C5-C10的直链烷烃和/或C5-C10的环烷烃。More preferably, the inert organic solvent comprises C5-C10 straight-chain alkanes and/or C5-C10 cycloalkanes.
更优选地,所述惰性有机溶剂包括正戊烷、正己烷、环己烷和正庚烷中的至少一种。More preferably, the inert organic solvent comprises at least one of n-pentane, n-hexane, cyclohexane and n-heptane.
优选地,步骤1)中所述有机溶剂的用量为:新癸酸钕:有机溶剂=0.3-0.6mol/L。Preferably, the amount of the organic solvent in step 1) is: neodymium neodecanoate: organic solvent = 0.3-0.6 mol/L.
本发明还涉及上述的新癸酸稀土催化剂或上述的制备方法制备得到的新癸酸稀土催化剂在制备聚丁二烯中的应用。The present invention also relates to the use of the neodecanoic acid rare earth catalyst or the neodecanoic acid rare earth catalyst prepared by the above preparation method in the preparation of polybutadiene.
优选地,制备聚丁二烯的方法如下:Preferably, the method for preparing polybutadiene is as follows:
在惰性气氛下,将所述新癸酸稀土催化剂和1,3-丁二烯单体在溶剂中混合,在40-70℃下进行聚合反应,即得。Under an inert atmosphere, the neodecanoic acid rare earth catalyst and 1,3-butadiene monomer are mixed in a solvent, and a polymerization reaction is carried out at 40-70° C. to obtain the product.
更优选地,所述溶剂为环己烷。More preferably, the solvent is cyclohexane.
更优选地,所述新癸酸稀土催化剂中的新癸酸钕与1,3-丁二烯单体的摩尔比为:2×10-5-6×10-5:1。More preferably, the molar ratio of neodymium neodecanoate to 1,3-butadiene monomer in the neodecanoate rare earth catalyst is 2×10 -5 -6×10 -5 :1.
更优选地,所述1,3-丁二烯单体与溶剂的用量比为1.5-2.5mol/L。More preferably, the usage ratio of the 1,3-butadiene monomer to the solvent is 1.5-2.5 mol/L.
更优选地,聚合反应的时间为1.5-2.5h。More preferably, the polymerization reaction time is 1.5-2.5 h.
更优选地,聚合反应采用本领域常用的终止剂进行终止,比如,可以为乙醇、异丙醇、2,6-二叔丁基对苯二酚甲醇中的至少一种。More preferably, the polymerization reaction is terminated using a terminator commonly used in the art, for example, at least one of ethanol, isopropanol, and 2,6-di-tert-butylhydroquinone methanol.
本发明的有益效果是:The beneficial effects of the present invention are:
本发明优化了稀土催化剂的组成,含卤素化合物、醇类化合物和助剂协同作用显著,显著提升了催化剂的催化活性和选择性,制备得到的聚丁二烯橡胶顺式结构含量更高,分子量较大同时分子量分布较窄,产品收率高。The present invention optimizes the composition of the rare earth catalyst, and the halogen-containing compound, the alcohol compound and the auxiliary agent have a significant synergistic effect, which significantly improves the catalytic activity and selectivity of the catalyst. The prepared polybutadiene rubber has a higher cis structure content, a larger molecular weight and a narrower molecular weight distribution, and a high product yield.
本发明进一步优化了助剂的组成,三苯基(甲基)-四(五氟苯)硼酸盐和苯基-二甲基氨基-四苯基硼酸盐协同作用显著,进一步提升了催化剂的催化活性和选择性,聚丁二烯橡胶产品收率、产品分子量、分子量分布效果和顺式结构立体选择性明显提高。The present invention further optimizes the composition of the auxiliary agent, triphenyl (methyl) -tetrakis (pentafluorobenzene) borate and phenyl - dimethylamino - tetraphenyl borate have a significant synergistic effect, further improves the catalytic activity and selectivity of the catalyst, and significantly improves the yield of the polybutadiene rubber product, the product molecular weight, the molecular weight distribution effect and the cis structure stereoselectivity.
具体实施方式DETAILED DESCRIPTION
下面结合具体实施例来进一步描述本发明,本发明的优点和特点将会随着描述而更为清楚。但这些实施例仅是范例性的,并不对本发明的范围构成任何限制。本领域技术人员应该理解的是,在不偏离本发明的精神和范围下可以对本发明技术方案的细节和形式进行修改或替换,但这些修改和替换均落入本发明的保护范围内。The present invention will be further described below in conjunction with specific embodiments, and the advantages and features of the present invention will become clearer as the description proceeds. However, these embodiments are merely exemplary and do not constitute any limitation to the scope of the present invention. It should be understood by those skilled in the art that the details and forms of the technical solution of the present invention may be modified or replaced without departing from the spirit and scope of the present invention, but these modifications and replacements all fall within the scope of protection of the present invention.
实施例1Example 1
一种新癸酸稀土催化剂,包括如下组分:新癸酸钕、含卤素化合物、醇类化合物、共轭二烯烃和助剂,新癸酸钕中的钕元素、含卤素化合物、醇类化合物、共轭二烯烃、助剂的摩尔比为1:1:5:20:1,助剂包括三苯基(甲基)-四(五氟苯)硼酸盐和苯基-二甲基氨基-四苯基硼酸盐的混合物,两者摩尔比2:1;A neodecanoate rare earth catalyst comprises the following components: neodymium neodecanoate, a halogen-containing compound, an alcohol compound, a conjugated diene and an auxiliary agent, wherein the molar ratio of the neodymium element, the halogen-containing compound, the alcohol compound, the conjugated diene and the auxiliary agent in the neodymium neodecanoate is 1:1:5:20:1, and the auxiliary agent comprises a mixture of triphenyl(methyl)-tetrakis(pentafluorobenzene)borate and phenyl-dimethylamino-tetraphenylborate, and the molar ratio of the two is 2:1;
含卤素化合物为一氯二乙基铝和三氯二异丁基铝的混合物,两者摩尔比1:1;The halogen-containing compound is a mixture of diethylaluminum monochloride and diisobutylaluminum trichloride, with a molar ratio of 1:1;
醇类化合物为异丙醇和环己醇的混合物,两者摩尔比3:1;The alcohol compound is a mixture of isopropanol and cyclohexanol, with a molar ratio of 3:1;
共轭二烯烃为异戊二烯。The conjugated diene is isoprene.
所述新癸酸钕的制备方法包括如下步骤:The preparation method of neodymium neodecanoate comprises the following steps:
(1)将23重量份氧化钕用盐酸溶解,控制pH为4.5,除杂质得到氯化钕NdCl3溶液;(1) dissolving 23 parts by weight of neodymium oxide in hydrochloric acid, controlling the pH to 4.5, and removing impurities to obtain a neodymium chloride NdCl 3 solution;
(2)将步骤(1)的NdCl3溶液静置,过滤沉淀,得到澄清的NdCl3溶液;(2) allowing the NdCl 3 solution of step (1) to stand, filtering and precipitating to obtain a clarified NdCl 3 solution;
(3)将170重量份新癸酸和185重量份正己烷混合,加入50重量份浓度为5mol/L的氢氧化钠溶液,在60℃下进行皂化反应35分钟得到反应液;(3) 170 parts by weight of neodecanoic acid and 185 parts by weight of n-hexane were mixed, 50 parts by weight of a 5 mol/L sodium hydroxide solution was added, and a saponification reaction was carried out at 60° C. for 35 minutes to obtain a reaction solution;
(4)将澄清的NdCl3溶液加入步骤(3)的反应液中,混合反应20分钟以上,静置分相;(4) adding the clarified NdCl 3 solution to the reaction solution of step (3), mixing and reacting for more than 20 minutes, and standing for phase separation;
(5)将步骤(4)上层成品进一步过滤,除杂质完成即得。(5) The upper layer of the finished product in step (4) is further filtered to remove impurities.
稀土催化剂的制备方法,包括如下步骤:The preparation method of the rare earth catalyst comprises the following steps:
1)在惰性气氛下,将新癸酸钕、醇类化合物、助剂和共轭二烯烃溶于正戊烷中,新癸酸钕:正戊烷=0.3mol/L,得到混合溶液A;1) Under an inert atmosphere, dissolving neodymium neodecanoate, an alcohol compound, an auxiliary agent and a conjugated diene in n-pentane, neodymium neodecanoate:n-pentane=0.3 mol/L, to obtain a mixed solution A;
2)在混合溶液A中加入含卤素化合物,得到混合溶液B,陈化15min即得。2) Add a halogen-containing compound to the mixed solution A to obtain a mixed solution B, and age it for 15 minutes.
实施例2Example 2
一种新癸酸稀土催化剂,包括如下组分:新癸酸钕、含卤素化合物、醇类化合物、共轭二烯烃和助剂,新癸酸钕中的钕元素、含卤素化合物、醇类化合物、共轭二烯烃、助剂的摩尔比为1:20:10:80:5,助剂包括三苯基(甲基)-四(五氟苯)硼酸盐和苯基-二甲基氨基-四苯基硼酸盐的混合物,两者摩尔比4:1;A neodecanoate rare earth catalyst comprises the following components: neodymium neodecanoate, a halogen-containing compound, an alcohol compound, a conjugated diene and an auxiliary agent, wherein the molar ratio of the neodymium element, the halogen-containing compound, the alcohol compound, the conjugated diene and the auxiliary agent in the neodymium neodecanoate is 1:20:10:80:5, and the auxiliary agent comprises a mixture of triphenyl(methyl)-tetrakis(pentafluorobenzene)borate and phenyl-dimethylamino-tetraphenylborate, and the molar ratio of the two is 4:1;
含卤素化合物为一氯二乙基铝和三氯二异丁基铝的混合物,两者摩尔比3:1;The halogen-containing compound is a mixture of diethylaluminum monochloride and diisobutylaluminum trichloride, with a molar ratio of 3:1;
醇类化合物为异丙醇和环己醇的混合物,两者摩尔比5:1;The alcohol compound is a mixture of isopropanol and cyclohexanol, with a molar ratio of 5:1;
共轭二烯烃为间戊二烯。The conjugated diene is piperylene.
所述新癸酸钕的制备方法包括如下步骤:The preparation method of neodymium neodecanoate comprises the following steps:
(1)将24重量份氧化钕用盐酸溶解,控制pH为5.0,除杂质得到氯化钕NdCl3溶液;(1) dissolving 24 parts by weight of neodymium oxide in hydrochloric acid, controlling the pH to 5.0, and removing impurities to obtain a neodymium chloride NdCl 3 solution;
(2)将步骤(1)的NdCl3溶液静置,过滤沉淀,得到澄清的NdCl3溶液;(2) allowing the NdCl 3 solution of step (1) to stand, filtering and precipitating to obtain a clarified NdCl 3 solution;
(3)将178重量份新癸酸和195重量份正己烷混合,加入55重量份浓度为5mol/L的氢氧化钠溶液,在65℃下进行皂化反应30分钟得到反应液;(3) 178 parts by weight of neodecanoic acid and 195 parts by weight of n-hexane were mixed, 55 parts by weight of a 5 mol/L sodium hydroxide solution was added, and a saponification reaction was carried out at 65° C. for 30 minutes to obtain a reaction solution;
(4)将澄清的NdCl3溶液加入步骤(3)的反应液中,混合反应20分钟以上,静置分相;(4) adding the clarified NdCl 3 solution to the reaction solution of step (3), mixing and reacting for more than 20 minutes, and standing for phase separation;
(5)将步骤(4)上层成品进一步过滤,除杂质完成即得。(5) The upper layer of the finished product in step (4) is further filtered to remove impurities.
稀土催化剂的制备方法,包括如下步骤:The preparation method of the rare earth catalyst comprises the following steps:
1)在惰性气氛下,将新癸酸钕、醇类化合物、助剂和共轭二烯烃溶于正庚烷中,新癸酸钕:正庚烷=0.6mol/L,得到混合溶液A;1) Under an inert atmosphere, dissolving neodymium neodecanoate, an alcohol compound, an auxiliary agent and a conjugated diene in n-heptane, neodymium neodecanoate: n-heptane = 0.6 mol/L, to obtain a mixed solution A;
2)在混合溶液A中加入含卤素化合物,得到混合溶液B,陈化30min即得。2) Add a halogen-containing compound to the mixed solution A to obtain a mixed solution B, and age it for 30 minutes.
实施例3Example 3
一种新癸酸稀土催化剂,包括如下组分:新癸酸钕、含卤素化合物、醇类化合物、共轭二烯烃和助剂,新癸酸钕中的钕元素、含卤素化合物、醇类化合物、共轭二烯烃、助剂的摩尔比为1:10:7:50:3,助剂包括三苯基(甲基)-四(五氟苯)硼酸盐和苯基-二甲基氨基-四苯基硼酸盐的混合物,两者摩尔比3:1;A neodecanoate rare earth catalyst comprises the following components: neodymium neodecanoate, a halogen-containing compound, an alcohol compound, a conjugated diene and an auxiliary agent, wherein the molar ratio of the neodymium element, the halogen-containing compound, the alcohol compound, the conjugated diene and the auxiliary agent in the neodymium neodecanoate is 1:10:7:50:3, and the auxiliary agent comprises a mixture of triphenyl(methyl)-tetrakis(pentafluorobenzene)borate and phenyl-dimethylamino-tetraphenylborate, and the molar ratio of the two is 3:1;
含卤素化合物为一氯二乙基铝和三氯二异丁基铝的混合物,两者摩尔比2:1;The halogen-containing compound is a mixture of diethylaluminum monochloride and diisobutylaluminum trichloride, with a molar ratio of 2:1;
醇类化合物为异丙醇和环己醇的混合物,两者摩尔比4:1;The alcohol compound is a mixture of isopropanol and cyclohexanol, with a molar ratio of 4:1;
共轭二烯烃为异戊二烯。The conjugated diene is isoprene.
所述新癸酸钕的制备方法包括如下步骤:The preparation method of neodymium neodecanoate comprises the following steps:
(1)将24重量份氧化钕用盐酸溶解,控制pH为4.5,除杂质得到氯化钕NdCl3溶液;(1) dissolving 24 parts by weight of neodymium oxide in hydrochloric acid, controlling the pH to 4.5, and removing impurities to obtain a neodymium chloride NdCl 3 solution;
(2)将步骤(1)的NdCl3溶液静置,过滤沉淀,得到澄清的NdCl3溶液;(2) allowing the NdCl 3 solution of step (1) to stand, filtering and precipitating to obtain a clarified NdCl 3 solution;
(3)将175重量份新癸酸和190重量份正己烷混合,加入53重量份浓度为5mol/L的氢氧化钠溶液,在65℃下进行皂化反应35分钟得到反应液;(3) 175 parts by weight of neodecanoic acid and 190 parts by weight of n-hexane were mixed, 53 parts by weight of a 5 mol/L sodium hydroxide solution was added, and a saponification reaction was carried out at 65° C. for 35 minutes to obtain a reaction solution;
(4)将澄清的NdCl3溶液加入步骤(3)的反应液中,混合反应20分钟以上,静置分相;(4) adding the clarified NdCl 3 solution to the reaction solution of step (3), mixing and reacting for more than 20 minutes, and standing for phase separation;
(5)将步骤(4)上层成品进一步过滤,除杂质完成即得。(5) The upper layer of the finished product in step (4) is further filtered to remove impurities.
稀土催化剂的制备方法,包括如下步骤:The preparation method of the rare earth catalyst comprises the following steps:
1)在惰性气氛下,将新癸酸钕、醇类化合物、助剂和共轭二烯烃溶于环己烷中,新癸酸钕:环己烷=0.5mol/L,得到混合溶液A;1) Under an inert atmosphere, dissolving neodymium neodecanoate, an alcohol compound, an auxiliary agent and a conjugated diene in cyclohexane, neodymium neodecanoate: cyclohexane = 0.5 mol/L, to obtain a mixed solution A;
2)在混合溶液A中加入含卤素化合物,得到混合溶液B,陈化20min即得。2) Add a halogen-containing compound to the mixed solution A to obtain a mixed solution B, and age it for 20 minutes.
对比例1Comparative Example 1
与实施例3的区别仅在于催化剂组成不同,各组分摩尔比具体如下:The only difference from Example 3 is the catalyst composition. The molar ratios of the components are as follows:
对比例2Comparative Example 2
与实施例3的区别仅在于助剂组成不同,替换为等摩尔量的甲基铝氧烷。The only difference from Example 3 is that the auxiliary agent composition is different, and is replaced by an equal molar amount of methylaluminoxane.
对比例3Comparative Example 3
与实施例3的区别仅在于助剂组成不同,将三苯基(甲基)-四(五氟苯)硼酸盐替换为等摩尔量的苯基-二甲基氨基-四苯基硼酸盐。The only difference from Example 3 is the auxiliary agent composition, in which triphenyl(methyl)-tetrakis(pentafluorophenyl)borate is replaced by an equimolar amount of phenyl-dimethylamino-tetraphenylborate.
对比例4Comparative Example 4
与实施例3的区别仅在于助剂组成不同,将苯基-二甲基氨基-四苯基硼酸盐替换为等摩尔量的三苯基(甲基)-四(五氟苯)硼酸盐。The only difference from Example 3 is the auxiliary agent composition, in which phenyl-dimethylamino-tetraphenylborate is replaced by an equimolar amount of triphenyl(methyl)-tetrakis(pentafluorophenyl)borate.
应用例Application Examples
聚丁二烯的制备方法:在氮气气氛下,将实施例1-3和对比例1-4任一新癸酸稀土催化剂和1,3-丁二烯单体在环己烷中混合,新癸酸钕与1,3-丁二烯单体的摩尔比为4×10-5:1,1,3-丁二烯单体与环己烷的用量比为2mol/L,在60℃下进行聚合反应2h,加入适量乙醇终止反应,干燥后即得。Preparation method of polybutadiene: Under nitrogen atmosphere, any neodecanoic acid rare earth catalyst of Examples 1-3 and Comparative Examples 1-4 and 1,3-butadiene monomer are mixed in cyclohexane, the molar ratio of neodymium neodecanoate to 1,3-butadiene monomer is 4×10 -5 :1, and the amount ratio of 1,3-butadiene monomer to cyclohexane is 2 mol/L. The polymerization reaction is carried out at 60° C. for 2 h, and an appropriate amount of ethanol is added to terminate the reaction. The product is obtained after drying.
测试例Test Case
测定应用例制备得到的聚丁二烯的收率、顺式结构含量、分子量和分子量分布,结果如表1所示。The yield, cis-structure content, molecular weight and molecular weight distribution of the polybutadiene prepared in the application example were measured. The results are shown in Table 1.
表1Table 1
由对比例1-1至对比例1-3可知,仅含有含卤素化合物、醇类化合物和助剂中的任意两种,聚丁二烯收率、顺式结构的立体选择性、产品分子量均显著降低,分子量分布明显变宽。说明本发明的含卤素化合物、醇类化合物和助剂之间协同作用显著,可以同时提高聚丁二烯收率、顺式结构的立体选择性、产品分子量和分子量分布方面的效果。From Comparative Examples 1-1 to 1-3, it can be seen that when only any two of the halogen-containing compound, the alcohol compound and the auxiliary agent are contained, the polybutadiene yield, the stereoselectivity of the cis structure, and the product molecular weight are significantly reduced, and the molecular weight distribution is significantly broadened. This shows that the halogen-containing compound, the alcohol compound and the auxiliary agent of the present invention have a significant synergistic effect, and can simultaneously improve the polybutadiene yield, the stereoselectivity of the cis structure, the product molecular weight and the molecular weight distribution.
由对比例2和实施例3对比可知,本发明的助剂替换为甲基铝氧烷以后,产品收率、顺式结构的立体选择性和分子量明显降低,尤其是分子量分布效果,降低了56.6%。From the comparison between Comparative Example 2 and Example 3, it can be seen that after the auxiliary agent of the present invention is replaced with methylaluminoxane, the product yield, stereoselectivity of the cis structure and the molecular weight are significantly reduced, especially the molecular weight distribution effect, which is reduced by 56.6%.
由对比例1-3、对比例3、对比例4和实施例3对比可知,对比例3和对比例4在对比例1-3的基础上添加了一种助剂,产品收率、产品分子量和分子量分布效果有所提高,但是对顺式结构的立体选择性影响较小。实施例3添加了两种助剂,结果顺式结构的立体选择性显著提高,同时进一步明显提高了分子量分布效果、收率和分子量,说明两种助剂协同作用显著。By comparing Comparative Examples 1-3, Comparative Example 3, Comparative Example 4 and Example 3, it can be seen that Comparative Examples 3 and Comparative Example 4 add an auxiliary agent on the basis of Comparative Examples 1-3, and the product yield, product molecular weight and molecular weight distribution effects are improved, but the stereoselectivity of the cis structure is less affected. Example 3 adds two auxiliary agents, and the stereoselectivity of the cis structure is significantly improved, and the molecular weight distribution effect, yield and molecular weight are further significantly improved, indicating that the two auxiliary agents have a significant synergistic effect.
上述详细说明是针对本发明其中之一可行实施例的具体说明,该实施例并非用以限制本发明的专利范围,凡未脱离本发明所为的等效实施或变更,均应包含于本发明技术方案的范围内。The above detailed description is a specific description of one feasible embodiment of the present invention. The embodiment is not intended to limit the patent scope of the present invention. Any equivalent implementation or modification that does not deviate from the present invention should be included in the scope of the technical solution of the present invention.
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Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20020057922A (en) * | 2002-06-14 | 2002-07-12 | 박찬구 | Polymerization method of high 1,4-cis polybutadine and its derivatives |
CN1568332A (en) * | 2001-10-12 | 2005-01-19 | 陶氏环球技术公司 | Metal complex compositions and their use as catalysts to produce polydienes |
CN102532365A (en) * | 2010-12-09 | 2012-07-04 | 中国石油化工股份有限公司 | Neodymium-based homogeneous phase rare earth catalyst and preparation method and application thereof |
JP2018104548A (en) * | 2016-12-26 | 2018-07-05 | 宇部興産株式会社 | Catalyst solution for conjugate diene polymerization and polymerization method therewith |
US10703837B1 (en) * | 2019-05-01 | 2020-07-07 | The Goodyear Tire & Rubber Company | Method of making a functionalized elastomer, elastomer, rubber composition and tire |
CN117264103A (en) * | 2023-11-21 | 2023-12-22 | 传化智联股份有限公司 | Rare earth catalyst containing neodecanoic acid neodymium and preparation method of polybutadiene based on catalyst |
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1568332A (en) * | 2001-10-12 | 2005-01-19 | 陶氏环球技术公司 | Metal complex compositions and their use as catalysts to produce polydienes |
KR20020057922A (en) * | 2002-06-14 | 2002-07-12 | 박찬구 | Polymerization method of high 1,4-cis polybutadine and its derivatives |
CN102532365A (en) * | 2010-12-09 | 2012-07-04 | 中国石油化工股份有限公司 | Neodymium-based homogeneous phase rare earth catalyst and preparation method and application thereof |
JP2018104548A (en) * | 2016-12-26 | 2018-07-05 | 宇部興産株式会社 | Catalyst solution for conjugate diene polymerization and polymerization method therewith |
US10703837B1 (en) * | 2019-05-01 | 2020-07-07 | The Goodyear Tire & Rubber Company | Method of making a functionalized elastomer, elastomer, rubber composition and tire |
CN117264103A (en) * | 2023-11-21 | 2023-12-22 | 传化智联股份有限公司 | Rare earth catalyst containing neodecanoic acid neodymium and preparation method of polybutadiene based on catalyst |
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