CN111333761A - Catalyst for preparing rare earth butadiene rubber and preparation method thereof - Google Patents
Catalyst for preparing rare earth butadiene rubber and preparation method thereof Download PDFInfo
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- 229910052761 rare earth metal Inorganic materials 0.000 title claims abstract description 61
- 239000003054 catalyst Substances 0.000 title claims abstract description 52
- 150000002910 rare earth metals Chemical class 0.000 title claims abstract description 46
- 239000005062 Polybutadiene Substances 0.000 title claims abstract description 41
- 229920002857 polybutadiene Polymers 0.000 title claims abstract description 41
- 238000002360 preparation method Methods 0.000 title claims abstract description 14
- -1 rare earth compounds Chemical class 0.000 claims abstract description 69
- 150000001638 boron Chemical class 0.000 claims abstract description 15
- 150000001993 dienes Chemical class 0.000 claims abstract description 15
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims description 19
- 239000011259 mixed solution Substances 0.000 claims description 16
- 229910052779 Neodymium Inorganic materials 0.000 claims description 15
- 229910052777 Praseodymium Inorganic materials 0.000 claims description 13
- 229910052684 Cerium Inorganic materials 0.000 claims description 12
- OEOIWYCWCDBOPA-UHFFFAOYSA-N 6-methyl-heptanoic acid Chemical compound CC(C)CCCCC(O)=O OEOIWYCWCDBOPA-UHFFFAOYSA-N 0.000 claims description 9
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 claims description 9
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 9
- 230000032683 aging Effects 0.000 claims description 7
- 239000011261 inert gas Substances 0.000 claims description 7
- 239000012442 inert solvent Substances 0.000 claims description 7
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 6
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 claims description 6
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 claims description 6
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 claims description 6
- QARVLSVVCXYDNA-UHFFFAOYSA-N bromobenzene Chemical compound BrC1=CC=CC=C1 QARVLSVVCXYDNA-UHFFFAOYSA-N 0.000 claims description 6
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 6
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims description 6
- MCULRUJILOGHCJ-UHFFFAOYSA-N triisobutylaluminium Chemical compound CC(C)C[Al](CC(C)C)CC(C)C MCULRUJILOGHCJ-UHFFFAOYSA-N 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 5
- 239000000243 solution Substances 0.000 claims description 5
- PUDIUYLPXJFUGB-UHFFFAOYSA-N praseodymium atom Chemical compound [Pr] PUDIUYLPXJFUGB-UHFFFAOYSA-N 0.000 claims description 4
- WQONPSCCEXUXTQ-UHFFFAOYSA-N 1,2-dibromobenzene Chemical compound BrC1=CC=CC=C1Br WQONPSCCEXUXTQ-UHFFFAOYSA-N 0.000 claims description 3
- OCJBOOLMMGQPQU-UHFFFAOYSA-N 1,4-dichlorobenzene Chemical compound ClC1=CC=C(Cl)C=C1 OCJBOOLMMGQPQU-UHFFFAOYSA-N 0.000 claims description 3
- UZGARMTXYXKNQR-UHFFFAOYSA-K 7,7-dimethyloctanoate;neodymium(3+) Chemical compound [Nd+3].CC(C)(C)CCCCCC([O-])=O.CC(C)(C)CCCCCC([O-])=O.CC(C)(C)CCCCCC([O-])=O UZGARMTXYXKNQR-UHFFFAOYSA-K 0.000 claims description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 3
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 3
- 229910052786 argon Inorganic materials 0.000 claims description 3
- SIPUZPBQZHNSDW-UHFFFAOYSA-N bis(2-methylpropyl)aluminum Chemical compound CC(C)C[Al]CC(C)C SIPUZPBQZHNSDW-UHFFFAOYSA-N 0.000 claims description 3
- GWXLDORMOJMVQZ-UHFFFAOYSA-N cerium Chemical compound [Ce] GWXLDORMOJMVQZ-UHFFFAOYSA-N 0.000 claims description 3
- FGWBAWJNMYHXMA-UHFFFAOYSA-K cerium(3+);7,7-dimethyloctanoate Chemical compound [Ce+3].CC(C)(C)CCCCCC([O-])=O.CC(C)(C)CCCCCC([O-])=O.CC(C)(C)CCCCCC([O-])=O FGWBAWJNMYHXMA-UHFFFAOYSA-K 0.000 claims description 3
- LBOJURZAODJTAG-UHFFFAOYSA-K cerium(3+);hexanoate Chemical compound [Ce+3].CCCCCC([O-])=O.CCCCCC([O-])=O.CCCCCC([O-])=O LBOJURZAODJTAG-UHFFFAOYSA-K 0.000 claims description 3
- 229940117389 dichlorobenzene Drugs 0.000 claims description 3
- YNLAOSYQHBDIKW-UHFFFAOYSA-M diethylaluminium chloride Chemical compound CC[Al](Cl)CC YNLAOSYQHBDIKW-UHFFFAOYSA-M 0.000 claims description 3
- 229910001873 dinitrogen Inorganic materials 0.000 claims description 3
- MGDOJPNDRJNJBK-UHFFFAOYSA-N ethylaluminum Chemical compound [Al].C[CH2] MGDOJPNDRJNJBK-UHFFFAOYSA-N 0.000 claims description 3
- 239000007789 gas Substances 0.000 claims description 3
- LLEHGVASIZFKRV-UHFFFAOYSA-K hexanoate praseodymium(3+) Chemical compound [Pr+3].CCCCCC([O-])=O.CCCCCC([O-])=O.CCCCCC([O-])=O LLEHGVASIZFKRV-UHFFFAOYSA-K 0.000 claims description 3
- KQFYWTSRWKUWMJ-UHFFFAOYSA-K hexanoate;neodymium(3+) Chemical compound [Nd+3].CCCCCC([O-])=O.CCCCCC([O-])=O.CCCCCC([O-])=O KQFYWTSRWKUWMJ-UHFFFAOYSA-K 0.000 claims description 3
- NRQNMMBQPIGPTB-UHFFFAOYSA-N methylaluminum Chemical compound [CH3].[Al] NRQNMMBQPIGPTB-UHFFFAOYSA-N 0.000 claims description 3
- QEFYFXOXNSNQGX-UHFFFAOYSA-N neodymium atom Chemical compound [Nd] QEFYFXOXNSNQGX-UHFFFAOYSA-N 0.000 claims description 3
- DZNFWGVDYGAMJB-UHFFFAOYSA-K neodymium(3+);phosphate Chemical compound [Nd+3].[O-]P([O-])([O-])=O DZNFWGVDYGAMJB-UHFFFAOYSA-K 0.000 claims description 3
- VOITXYVAKOUIBA-UHFFFAOYSA-N triethylaluminium Chemical compound CC[Al](CC)CC VOITXYVAKOUIBA-UHFFFAOYSA-N 0.000 claims description 3
- ORYGRKHDLWYTKX-UHFFFAOYSA-N trihexylalumane Chemical compound CCCCCC[Al](CCCCCC)CCCCCC ORYGRKHDLWYTKX-UHFFFAOYSA-N 0.000 claims description 3
- JLTRXTDYQLMHGR-UHFFFAOYSA-N trimethylaluminium Chemical compound C[Al](C)C JLTRXTDYQLMHGR-UHFFFAOYSA-N 0.000 claims description 3
- 239000008096 xylene Substances 0.000 claims description 3
- LBGZJZYQLMTOBU-UHFFFAOYSA-K [Pr+3].CC(C)(C)CCCCCC([O-])=O.CC(C)(C)CCCCCC([O-])=O.CC(C)(C)CCCCCC([O-])=O Chemical compound [Pr+3].CC(C)(C)CCCCCC([O-])=O.CC(C)(C)CCCCCC([O-])=O.CC(C)(C)CCCCCC([O-])=O LBGZJZYQLMTOBU-UHFFFAOYSA-K 0.000 claims description 2
- 229910052782 aluminium Inorganic materials 0.000 claims description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 5
- 230000003197 catalytic effect Effects 0.000 abstract description 4
- 239000000178 monomer Substances 0.000 abstract description 2
- 238000006116 polymerization reaction Methods 0.000 description 4
- 150000001336 alkenes Chemical class 0.000 description 3
- 125000005234 alkyl aluminium group Chemical group 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 2
- 239000002861 polymer material Substances 0.000 description 2
- 239000005060 rubber Substances 0.000 description 2
- YPIFGDQKSSMYHQ-UHFFFAOYSA-N 7,7-dimethyloctanoic acid Chemical compound CC(C)(C)CCCCCC(O)=O YPIFGDQKSSMYHQ-UHFFFAOYSA-N 0.000 description 1
- 244000043261 Hevea brasiliensis Species 0.000 description 1
- 241001441571 Hiodontidae Species 0.000 description 1
- 230000003679 aging effect Effects 0.000 description 1
- 239000003426 co-catalyst Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012968 metallocene catalyst Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229920003052 natural elastomer Polymers 0.000 description 1
- 229920001194 natural rubber Polymers 0.000 description 1
- 238000004634 pharmacological analysis method Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 230000037048 polymerization activity Effects 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 238000004088 simulation Methods 0.000 description 1
- 230000035882 stress Effects 0.000 description 1
- 229920003048 styrene butadiene rubber Polymers 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 229920001059 synthetic polymer Polymers 0.000 description 1
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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
- C08F136/00—Homopolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds
- C08F136/02—Homopolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds
- C08F136/04—Homopolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds conjugated
- C08F136/06—Butadiene
-
- 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
- C08F136/00—Homopolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds
- C08F136/02—Homopolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds
- C08F136/04—Homopolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds conjugated
- C08F136/08—Isoprene
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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)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
Abstract
本发明属于制备顺丁橡胶的催化剂技术领域,公开了一种制备稀土顺丁橡胶的催化剂及制备方法,所述制备稀土顺丁橡胶的催化剂组分包括:有机稀土化合物、共轭二烯烃、有机硼盐、烷基铝化合物、分子量调节剂;所述有机稀土化合物、共轭二烯烃、有机硼盐、烷基铝化合物、分子量调节剂的摩尔比为5~20:10~50:1~5:10~30:30~50。本发明提供的制备稀土顺丁橡胶的催化剂及制备方法,在加烷基铝化合物之前加入分子量调节剂并陈化能形成均相、流动性好的催化体系,同时催化剂结构明确,易于合成,催化体系活性高,用量少,反应条件温和,能够有效提高稀土顺丁橡胶的单体转化率。
The invention belongs to the technical field of catalysts for preparing cis-butadiene rubber, and discloses a catalyst for preparing rare-earth cis-butadiene rubber and a preparation method. The catalyst components for preparing rare-earth cis-butadiene rubber include: organic rare earth compounds, conjugated dienes, organic Boron salt, alkyl aluminum compound, molecular weight regulator; the molar ratio of the organic rare earth compound, conjugated diene, organic boron salt, alkyl aluminum compound, and molecular weight regulator is 5-20:10-50:1-5 : 10~30: 30~50. In the catalyst and preparation method for preparing rare earth butadiene rubber provided by the invention, a molecular weight regulator is added and aged before the alkyl aluminum compound is added to form a catalytic system with a homogeneous phase and good fluidity. The system has high activity, less dosage and mild reaction conditions, which can effectively improve the monomer conversion rate of rare earth butadiene rubber.
Description
技术领域technical field
本发明属于制备顺丁橡胶的催化剂技术领域,尤其涉及一种制备稀土顺丁橡胶的催化剂及制备方法。The invention belongs to the technical field of catalysts for preparing cis-butadiene rubber, in particular to a catalyst for preparing rare earth cis-butadiene rubber and a preparation method.
背景技术Background technique
目前,最接近的现有技术:稀土顺丁橡胶在强度、定伸应力、伸长率等物理机械性能等方面明显优于普通的稀土顺丁橡胶。窄分子量分布(分布1.3~2.5)稀土顺丁橡胶在制作轮胎的过程中不但具有较佳的回弹性和压缩生热,而且在耐切割和耐裂口增长方面优势明显;由于硫化胶模量较低门尼稀土胶模量高,这有利于改进胎面胶的高温操控性。此外在溶聚丁苯胶/天然胶/顺丁橡胶三胶并用体系中,窄分子量分布(1.3~2.5)稀土顺丁橡胶综合性能好,动态力学性能、热氧老化性能高,耐切割和耐裂口增长性能突出,因此分子量分布(1.3~2.5)稀土顺丁橡胶的前景非常广阔。At present, the closest existing technology: rare earth butadiene rubber is obviously superior to ordinary rare earth butadiene rubber in terms of strength, constant elongation stress, elongation and other physical and mechanical properties. Narrow molecular weight distribution (distribution 1.3-2.5) rare earth butadiene rubber not only has better resilience and compression heat generation in the process of making tires, but also has obvious advantages in cutting resistance and crack growth resistance; due to the low modulus of vulcanizate Mooney rare earth rubber has a high modulus, which is conducive to improving the high temperature handling of the tread rubber. In addition, in the combined system of solution-polymerized styrene-butadiene rubber/natural rubber/cis-butadiene rubber, the narrow molecular weight distribution (1.3-2.5) rare earth cis-butadiene rubber has good comprehensive properties, high dynamic mechanical properties, high thermal-oxidative aging properties, cutting resistance and resistance to cutting. The crack growth performance is outstanding, so the prospect of rare earth butadiene rubber with molecular weight distribution (1.3 to 2.5) is very broad.
现有稀土催化剂主要有ziegler-Natta型稀土催化剂、茂稀土型催化剂以及非茂稀土型催化剂,Ziegler-Natta型催化体系是最早发现并用于烯烃聚合,目前发展最为成熟并己被广泛应用于工业的一类催化剂,其为烯烃聚合提供了高选择性,以(已)得到众多重要的合成聚合物材料。但由于其自身的缺点如多活性中心,使合成的聚合物具有相对较宽的分子量分布,导致聚合物材料性能具有一定的缺陷,在工业应用中存在一定的缺点;非均相,即催化剂的溶解性低,导致催化剂的使用率低,进而影响聚合活性等。茂稀土型催化剂在工业化的应用上也显示出了一定的弊端,主要的为合成茂金属催化剂的成本较高,同时助催化剂烷氧基铝的价格也比较昂贵;其次,茂金属催化剂在现有的仪器设备上合成形态好的烯烃聚合物必须要进行负载。非茂稀土化合物本身也存在缺点与不足,由于其耐温性差,作为烯烃聚合的催化剂其活性会随着聚合温度的升高而呈现降低的现象。The existing rare earth catalysts mainly include ziegler-Natta type rare earth catalysts, rare earth locene type catalysts and non-rare earth locene type catalysts. The Ziegler-Natta type catalyst system was the first to be discovered and used for olefin polymerization. At present, it is the most mature and has been widely used in industry. A class of catalysts that provide high selectivity for the polymerization of olefins to (have) yielded numerous important synthetic polymer materials. However, due to its own shortcomings such as multiple active centers, the synthesized polymer has a relatively wide molecular weight distribution, resulting in certain defects in the performance of polymer materials, and there are certain shortcomings in industrial applications; heterogeneous, that is, the catalyst's Low solubility leads to low catalyst usage rate, which in turn affects polymerization activity. Rare earth-based catalysts also show certain drawbacks in industrial application. The main ones are that the cost of synthesizing metallocene catalysts is relatively high, and the price of aluminum alkoxides as co-catalysts is also relatively expensive. The olefin polymer in good shape synthesized on the equipment must be loaded. The non-rare earth locene compound itself also has shortcomings and deficiencies. Due to its poor temperature resistance, its activity as a catalyst for olefin polymerization will decrease with the increase of polymerization temperature.
综上所述,现有技术存在的问题是:现有稀土催化剂都具备一定的缺陷,在工业应用上具备较大的限制,耐温性差,制备成本高,催化剂溶解性能低、催化效率低。To sum up, the problems existing in the prior art are: the existing rare earth catalysts all have certain defects, and have large limitations in industrial application, poor temperature resistance, high preparation cost, low catalyst solubility, and low catalytic efficiency.
发明内容SUMMARY OF THE INVENTION
针对现有技术存在的问题,本发明提供了一种制备稀土顺丁橡胶的催化剂及制备方法。Aiming at the problems existing in the prior art, the present invention provides a catalyst for preparing rare earth butadiene rubber and a preparation method.
本发明是这样实现的,一种制备稀土顺丁橡胶的催化剂及制备方法,所述制备稀土顺丁橡胶的催化剂组分包括:有机稀土化合物、共轭二烯烃、有机硼盐、烷基铝化合物、分子量调节剂;The present invention is achieved in this way, a catalyst for preparing rare earth cis-butadiene rubber and a preparation method, the catalyst components for preparing rare earth cis-butadiene rubber include: organic rare earth compounds, conjugated dienes, organic boron salts, and alkyl aluminum compounds , Molecular weight regulator;
所述有机稀土化合物、共轭二烯烃、有机硼盐、烷基铝化合物、分子量调节剂的摩尔比为5~20:10~50:1~5:10~30:30~50。The molar ratio of the organic rare earth compound, the conjugated diene, the organic boron salt, the alkyl aluminum compound, and the molecular weight regulator is 5-20:10-50:1-5:10-30:30-50.
进一步,所述有机稀土化合物为磷酸钕、羧酸钕、羧酸镨或羧酸铈中的一种;所述羧酸钕为含有羧基的有机酸钕化合物,所述羧酸镨为含有羧基的有机酸镨化合物,所述羧酸铈为含有羧基的有机酸铈化合物。Further, the organic rare earth compound is one of neodymium phosphate, neodymium carboxylate, praseodymium carboxylate or cerium carboxylate; the neodymium carboxylate is an organic acid neodymium compound containing a carboxyl group, and the praseodymium carboxylate is a carboxyl group-containing neodymium carboxylate compound. The organic acid praseodymium compound, the cerium carboxylate is an organic acid cerium compound containing a carboxyl group.
进一步,所述含有羧基的有机酸钕化合物为新癸酸钕、环烷酸钕、异辛酸钕或己酸钕中的至少一种;所述含有羧基的有机酸镨化合物为新癸酸镨、环烷酸镨、异辛酸镨或己酸镨中的至少一种;所述含有羧基的有机酸铈化合物为新癸酸铈、环烷酸铈、异辛酸铈或己酸铈中的至少一种。Further, the carboxyl-containing organic acid neodymium compound is at least one of neodymium neodecanoate, neodymium naphthenate, neodymium isooctanoate or neodymium hexanoate; the carboxyl-containing organic acid praseodymium compound is praseodymium neodecanoate, At least one of praseodymium naphthenate, praseodymium isooctanoate or praseodymium hexanoate; the organic acid cerium compound containing a carboxyl group is at least one of cerium neodecanoate, cerium naphthenate, cerium isooctanoate or cerium hexanoate .
进一步,所述共轭二烯烃为异戊二烯、丁二烯中的一种或多种。Further, the conjugated diene is one or more of isoprene and butadiene.
进一步,所述有机硼盐为[B(C6H5)3]、[Ph3C][B(C6H5)4]、[PhNMe2][B(C6H5)4]和/或[Ph3C][B(C6F5)]4。Further, the organic boron salts are [B(C 6 H 5 ) 3 ], [Ph 3 C][B(C 6 H 5 ) 4 ], [PhNMe 2 ][B(C 6 H 5 ) 4 ] and /or [Ph 3 C][B(C 6 F 5 )] 4 .
进一步,所述分子量调节剂为三甲基铝、三乙基铝或三异丁基铝中的其中一种或多多种。Further, the molecular weight regulator is one or more of trimethylaluminum, triethylaluminum or triisobutylaluminum.
进一步,所述烷基铝化合物为甲基铝、乙基铝、三异丁基铝、氢化二异丁基铝、三己基铝和一氯二乙基铝中的至少一种。Further, the alkylaluminum compound is at least one of methylaluminum, ethylaluminum, triisobutylaluminum, diisobutylaluminum hydride, trihexylaluminum, and diethylaluminum monochloride.
本发明的另一目的在于提供一种所述稀土顺丁橡胶的催化剂的制备方法,所述稀土顺丁橡胶的催化剂制备方法包括以下步骤:Another object of the present invention is to provide a method for preparing the catalyst of the rare earth cis-butadiene rubber, and the method for preparing the catalyst of the rare earth cis-butadiene rubber comprises the following steps:
步骤一,在惰性气体的保护下,在惰性溶剂的存在下,向经干燥处理的催化剂陈化瓶中依次加入有机稀土化合物、共轭二烯烃、有机硼盐,在30℃的环境下陈化10-40分钟,得混合溶液A;Step 1, under the protection of inert gas and in the presence of inert solvent, add organic rare earth compound, conjugated diene and organic boron salt to the dried catalyst aging bottle in turn, and age at 30°C. 10-40 minutes, get mixed solution A;
步骤二,在步骤一得到的混合溶液A中加入分子量调节剂,在30℃的环境下陈化2-10小时,得混合溶液B;In step 2, a molecular weight regulator is added to the mixed solution A obtained in step 1, and the mixture is aged for 2-10 hours at a temperature of 30° C. to obtain a mixed solution B;
步骤三,在步骤二的混合溶液B形成均相透明溶液后再加入烷基铝化合物,在30℃的环境下陈化10-20小时,得到制备稀土顺丁橡胶的催化剂。In step 3, after the mixed solution B in step 2 forms a homogeneous transparent solution, the alkyl aluminum compound is added, and the mixture is aged at 30° C. for 10-20 hours to obtain a catalyst for preparing rare earth cis-butadiene rubber.
进一步,步骤一中,所述惰性溶剂包括:正己烷、正庚烷、正辛烷、甲苯、二甲苯、乙苯、氯苯、二氯苯、溴苯和二溴苯中的其中一种。Further, in step 1, the inert solvent includes one of n-hexane, n-heptane, n-octane, toluene, xylene, ethylbenzene, chlorobenzene, dichlorobenzene, bromobenzene and dibromobenzene.
进一步,步骤一中,所述惰性气体包括:氮气、氩气的其中一种。Further, in step 1, the inert gas includes one of nitrogen gas and argon gas.
综上所述,本发明的优点及积极效果为:本发明提供的制备稀土顺丁橡胶的催化剂及制备方法,在加烷基铝化合物之前加入分子量调节剂并陈化能形成均相、流动性好的催化体系,同时催化剂结构明确,易于合成,催化体系活性高,用量少,反应条件温和,能够有效提高稀土顺丁橡胶的单体转化率。To sum up, the advantages and positive effects of the present invention are as follows: the catalyst and preparation method for preparing rare earth butadiene rubber provided by the present invention can form a homogeneous phase and fluidity by adding a molecular weight regulator and aging before adding the alkyl aluminum compound. A good catalytic system, at the same time the catalyst structure is clear, easy to synthesize, high catalytic system activity, less dosage, mild reaction conditions, can effectively improve the monomer conversion rate of rare earth butadiene rubber.
附图说明Description of drawings
图1是本发明实施例提供的制备稀土顺丁橡胶的催化剂及制备方法。FIG. 1 is a catalyst and a preparation method for preparing rare earth butadiene rubber provided by an embodiment of the present invention.
图2是本发明实施例提供的催化剂反应温度对催化剂活性的影响示意图。FIG. 2 is a schematic diagram showing the influence of the catalyst reaction temperature on the catalyst activity provided by the embodiment of the present invention.
具体实施方式Detailed ways
为了使本发明的目的、技术方案及优点更加清楚明白,以下结合实施例,对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅仅用以解释本发明,并不用于限定本发明。In order to make the objectives, technical solutions and advantages of the present invention clearer, the present invention will be further described in detail below with reference to the embodiments. It should be understood that the specific embodiments described herein are only used to explain the present invention, but not to limit the present invention.
针对现有技术存在的问题,本发明提供了一种制备稀土顺丁橡胶的催化剂及制备方法,下面结合附图对本发明作详细的描述。In view of the problems existing in the prior art, the present invention provides a catalyst for preparing rare earth cis-butadiene rubber and a preparation method. The present invention is described in detail below with reference to the accompanying drawings.
本发明实施例提供的制备稀土顺丁橡胶的催化剂组分包括:有机稀土化合物、共轭二烯烃、有机硼盐、烷基铝化合物、分子量调节剂。The catalyst components for preparing rare earth butadiene rubber provided in the embodiment of the present invention include: organic rare earth compounds, conjugated dienes, organic boron salts, alkyl aluminum compounds, and molecular weight regulators.
本发明实施例提供的有机稀土化合物、共轭二烯烃、有机硼盐、烷基铝化合物、分子量调节剂的摩尔比为5~20:10~50:1~5:10~30:30~50。The molar ratio of the organic rare earth compound, the conjugated diene, the organic boron salt, the alkyl aluminum compound, and the molecular weight regulator provided in the embodiment of the present invention is 5-20:10-50:1-5:10-30:30-50 .
本发明实施例提供的有机稀土化合物为磷酸钕、羧酸钕、羧酸镨或羧酸铈中的一种;所述羧酸钕为含有羧基的有机酸钕化合物,所述羧酸镨为含有羧基的有机酸镨化合物,所述羧酸铈为含有羧基的有机酸铈化合物。The organic rare earth compound provided in the embodiment of the present invention is one of neodymium phosphate, neodymium carboxylate, praseodymium carboxylate or cerium carboxylate; the neodymium carboxylate is a neodymium organic acid compound containing a carboxyl group, and the praseodymium carboxylate is a neodymium carboxylate compound containing a carboxyl group. The organic acid praseodymium compound of a carboxyl group, and the cerium carboxylate is an organic acid cerium compound containing a carboxyl group.
本发明实施例提供的含有羧基的有机酸钕化合物为新癸酸钕、环烷酸钕、异辛酸钕或己酸钕中的至少一种;所述含有羧基的有机酸镨化合物为新癸酸镨、环烷酸镨、异辛酸镨或己酸镨中的至少一种;所述含有羧基的有机酸铈化合物为新癸酸铈、环烷酸铈、异辛酸铈或己酸铈中的至少一种。The carboxyl-containing organic acid neodymium compound provided in the embodiment of the present invention is at least one of neodymium neodecanoate, neodymium naphthenate, neodymium isooctanoate or neodymium hexanoate; the carboxyl-containing organic acid praseodymium compound is neodecanoic acid At least one of praseodymium, praseodymium naphthenate, praseodymium isooctanoate or praseodymium hexanoate; the organic acid cerium compound containing a carboxyl group is at least one of cerium neodecanoate, cerium naphthenate, cerium isooctanoate or cerium hexanoate A sort of.
本发明实施例提供的共轭二烯烃为异戊二烯、丁二烯中的一种或多种。The conjugated diene provided in the embodiment of the present invention is one or more of isoprene and butadiene.
本发明实施例提供的有机硼盐为[B(C6H5)3]、[Ph3C][B(C6H5)4]、[PhNMe2][B(C6H5)4]和/或[Ph3C][B(C6F5)]4。The organic boron salts provided in the embodiments of the present invention are [B(C 6 H 5 ) 3 ], [Ph 3 C][B(C 6 H 5 ) 4 ], [PhNMe 2 ][B(C 6 H 5 ) 4 ] and/or [Ph 3 C][B(C 6 F 5 )] 4 .
本发明实施例提供的分子量调节剂为三甲基铝、三乙基铝或三异丁基铝中的其中一种或多种。The molecular weight regulator provided in the embodiment of the present invention is one or more of trimethylaluminum, triethylaluminum or triisobutylaluminum.
本发明实施例提供的烷基铝化合物为甲基铝、乙基铝、三异丁基铝、氢化二异丁基铝、三己基铝和一氯二乙基铝中的至少一种。The alkylaluminum compound provided in the embodiment of the present invention is at least one of methylaluminum, ethylaluminum, triisobutylaluminum, diisobutylaluminum hydride, trihexylaluminum, and diethylaluminum monochloride.
如图1所示,本发明实施例提供的制备稀土顺丁橡胶的催化剂及制备方法包括以下步骤:As shown in Figure 1, the catalyst and preparation method for preparing rare earth cis-butadiene rubber provided by the embodiment of the present invention include the following steps:
S101,在惰性气体的保护下,在惰性溶剂的存在下,向经干燥处理的催化剂陈化瓶中依次加入有机稀土化合物、共轭二烯烃、有机硼盐,在30℃的环境下陈化10-40分钟,得混合溶液A。S101, under the protection of an inert gas and in the presence of an inert solvent, add organic rare earth compounds, conjugated dienes, and organic boron salts to the dried catalyst aging bottle in sequence, and age at 30°C for 10 -40 minutes to get mixed solution A.
S102,在步骤S101得到的混合溶液A中加入分子量调节剂,在30℃的环境下陈化2-10小时,得混合溶液B。S102, adding a molecular weight regulator to the mixed solution A obtained in step S101, and aging for 2-10 hours in an environment of 30° C. to obtain a mixed solution B.
S103,在步骤S102的混合溶液B形成均相透明溶液后再加入烷基铝化合物,在30℃的环境下陈化10-20小时,得到制备稀土顺丁橡胶的催化剂。S103 , after the mixed solution B in step S102 forms a homogeneous transparent solution, the alkyl aluminum compound is added, and the mixture is aged at 30° C. for 10-20 hours to obtain a catalyst for preparing rare earth butadiene rubber.
步骤S101中,本发明实施例提供的惰性溶剂包括:正己烷、正庚烷、正辛烷、甲苯、二甲苯、乙苯、氯苯、二氯苯、溴苯和二溴苯中的其中一种。In step S101, the inert solvent provided in the embodiment of the present invention includes: one of n-hexane, n-heptane, n-octane, toluene, xylene, ethylbenzene, chlorobenzene, dichlorobenzene, bromobenzene and dibromobenzene. kind.
步骤S101中,本发明实施例提供的惰性气体包括:氮气、氩气的其中一种。In step S101, the inert gas provided in the embodiment of the present invention includes one of nitrogen gas and argon gas.
下面结合试验对本发明的技术效果作进一步说明。The technical effects of the present invention will be further described below in conjunction with experiments.
(1)在惰性气体的保护下,在惰性溶剂的存在下,向经干燥处理的催化剂陈化瓶中依次加入有机稀土化合物、共轭二烯烃、有机硼盐,分别在10、20、30、40℃的环境下陈化10-40分钟,得混合溶液A;(1) Under the protection of inert gas, in the presence of inert solvent, add organic rare earth compound, conjugated diene, and organic boron salt to the dried catalyst aging bottle in turn, at 10, 20, 30, Aged for 10-40 minutes at 40°C to obtain mixed solution A;
(2)在步骤一得到的混合溶液A中加入分子量调节剂,在30℃的环境下陈化2-10小时,得混合溶液B;(2) adding a molecular weight regulator to the mixed solution A obtained in step 1, and ageing for 2-10 hours in an environment of 30° C. to obtain a mixed solution B;
(3)在步骤二的混合溶液B形成均相透明溶液后再加入烷基铝化合物,在30℃的环境下陈化10-20小时,得到制备稀土顺丁橡胶的催化剂。(3) After the mixed solution B in step 2 forms a homogeneous transparent solution, the alkyl aluminum compound is added, and the mixture is aged at 30° C. for 10-20 hours to obtain a catalyst for preparing rare earth cis-butadiene rubber.
证明部分(具体实施例/实验/仿真/药理学分析/能够证明本发明创造性的正面实验数据、证据材料、鉴定报告、商业数据、研发证据、商业合作证据等)Proof part (specific examples/experiments/simulation/pharmacological analysis/positive experimental data, evidence materials, appraisal reports, business data, research and development evidence, business cooperation evidence, etc. that can prove the inventiveness of the present invention)
以上所述仅为本发明的较佳实施例而已,并不用以限制本发明,凡在本发明的精神和原则之内所作的任何修改、等同替换和改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention and are not intended to limit the present invention. Any modifications, equivalent replacements and improvements made within the spirit and principles of the present invention shall be included in the protection of the present invention. within the range.
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