CN108484392A - The method that choline eutectic ionic liquid catalyzed alcoholysis polyethylene terephthalate prepares Di-2-ethylhexyl terephthalate - Google Patents
The method that choline eutectic ionic liquid catalyzed alcoholysis polyethylene terephthalate prepares Di-2-ethylhexyl terephthalate Download PDFInfo
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- 229920000139 polyethylene terephthalate Polymers 0.000 title claims abstract description 95
- 239000005020 polyethylene terephthalate Substances 0.000 title claims abstract description 95
- 239000002608 ionic liquid Substances 0.000 title claims abstract description 40
- 230000005496 eutectics Effects 0.000 title claims abstract description 37
- 238000000034 method Methods 0.000 title claims abstract description 24
- -1 polyethylene terephthalate Polymers 0.000 title claims abstract description 16
- 238000006136 alcoholysis reaction Methods 0.000 title claims abstract description 8
- 229960001231 choline Drugs 0.000 title abstract description 28
- OEYIOHPDSNJKLS-UHFFFAOYSA-N choline Chemical compound C[N+](C)(C)CCO OEYIOHPDSNJKLS-UHFFFAOYSA-N 0.000 title abstract description 28
- 239000002994 raw material Substances 0.000 claims abstract description 78
- 239000003054 catalyst Substances 0.000 claims abstract description 74
- KFROBPVFLIZCHZ-UHFFFAOYSA-N bis(6-methylheptyl) benzene-1,4-dicarboxylate Chemical compound CC(C)CCCCCOC(=O)C1=CC=C(C(=O)OCCCCCC(C)C)C=C1 KFROBPVFLIZCHZ-UHFFFAOYSA-N 0.000 claims abstract description 63
- 238000006243 chemical reaction Methods 0.000 claims abstract description 46
- 239000001763 2-hydroxyethyl(trimethyl)azanium Substances 0.000 claims abstract description 32
- 235000019743 Choline chloride Nutrition 0.000 claims abstract description 32
- 229960003178 choline chloride Drugs 0.000 claims abstract description 32
- SGMZJAMFUVOLNK-UHFFFAOYSA-M choline chloride Chemical compound [Cl-].C[N+](C)(C)CCO SGMZJAMFUVOLNK-UHFFFAOYSA-M 0.000 claims abstract description 30
- BWDBEAQIHAEVLV-UHFFFAOYSA-N 6-methylheptan-1-ol Chemical compound CC(C)CCCCCO BWDBEAQIHAEVLV-UHFFFAOYSA-N 0.000 claims abstract description 27
- 229910052751 metal Inorganic materials 0.000 claims abstract description 9
- 239000002184 metal Substances 0.000 claims abstract description 9
- 150000003839 salts Chemical class 0.000 claims abstract description 8
- 239000002904 solvent Substances 0.000 claims abstract description 8
- 230000035484 reaction time Effects 0.000 claims abstract description 7
- 230000015572 biosynthetic process Effects 0.000 claims description 40
- 238000003786 synthesis reaction Methods 0.000 claims description 40
- 230000015556 catabolic process Effects 0.000 claims description 24
- 238000006731 degradation reaction Methods 0.000 claims description 24
- ZOIORXHNWRGPMV-UHFFFAOYSA-N acetic acid;zinc Chemical compound [Zn].CC(O)=O.CC(O)=O ZOIORXHNWRGPMV-UHFFFAOYSA-N 0.000 claims description 21
- 239000004246 zinc acetate Substances 0.000 claims description 21
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 claims description 16
- ONDPHDOFVYQSGI-UHFFFAOYSA-N zinc nitrate Chemical compound [Zn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ONDPHDOFVYQSGI-UHFFFAOYSA-N 0.000 claims description 12
- 239000011592 zinc chloride Substances 0.000 claims description 8
- 235000005074 zinc chloride Nutrition 0.000 claims description 8
- XTVVROIMIGLXTD-UHFFFAOYSA-N copper(II) nitrate Chemical compound [Cu+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O XTVVROIMIGLXTD-UHFFFAOYSA-N 0.000 claims description 6
- 229940071125 manganese acetate Drugs 0.000 claims description 6
- UOGMEBQRZBEZQT-UHFFFAOYSA-L manganese(2+);diacetate Chemical compound [Mn+2].CC([O-])=O.CC([O-])=O UOGMEBQRZBEZQT-UHFFFAOYSA-L 0.000 claims description 6
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 claims description 6
- 229960001763 zinc sulfate Drugs 0.000 claims description 6
- 229910000368 zinc sulfate Inorganic materials 0.000 claims description 6
- 238000002360 preparation method Methods 0.000 abstract description 4
- 229910052739 hydrogen Inorganic materials 0.000 abstract description 3
- 239000001257 hydrogen Substances 0.000 abstract description 3
- 239000008187 granular material Substances 0.000 description 18
- 239000004014 plasticizer Substances 0.000 description 6
- 239000002699 waste material Substances 0.000 description 6
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 4
- HJJPJSXJAXAIPN-UHFFFAOYSA-N arecoline Chemical compound COC(=O)C1=CCCN(C)C1 HJJPJSXJAXAIPN-UHFFFAOYSA-N 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- KBPLFHHGFOOTCA-UHFFFAOYSA-N 1-Octanol Chemical compound CCCCCCCCO KBPLFHHGFOOTCA-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- WOZVHXUHUFLZGK-UHFFFAOYSA-N dimethyl terephthalate Chemical compound COC(=O)C1=CC=C(C(=O)OC)C=C1 WOZVHXUHUFLZGK-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- LYCAIKOWRPUZTN-UHFFFAOYSA-N ethylene glycol Natural products OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 235000010755 mineral Nutrition 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 239000004800 polyvinyl chloride Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 235000013904 zinc acetate Nutrition 0.000 description 2
- RWPICVVBGZBXNA-BGYRXZFFSA-N Bis(2-ethylhexyl) terephthalate Natural products CCCC[C@H](CC)COC(=O)C1=CC=C(C(=O)OC[C@H](CC)CCCC)C=C1 RWPICVVBGZBXNA-BGYRXZFFSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- RWPICVVBGZBXNA-UHFFFAOYSA-N bis(2-ethylhexyl) benzene-1,4-dicarboxylate Chemical compound CCCCC(CC)COC(=O)C1=CC=C(C(=O)OCC(CC)CCCC)C=C1 RWPICVVBGZBXNA-UHFFFAOYSA-N 0.000 description 1
- YHWCPXVTRSHPNY-UHFFFAOYSA-N butan-1-olate;titanium(4+) Chemical compound [Ti+4].CCCC[O-].CCCC[O-].CCCC[O-].CCCC[O-] YHWCPXVTRSHPNY-UHFFFAOYSA-N 0.000 description 1
- 235000014171 carbonated beverage Nutrition 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 238000010668 complexation reaction Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- 239000000374 eutectic mixture Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 150000008040 ionic compounds Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 231100000053 low toxicity Toxicity 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000011973 solid acid Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 235000013616 tea Nutrition 0.000 description 1
- LXEJRKJRKIFVNY-UHFFFAOYSA-N terephthaloyl chloride Chemical compound ClC(=O)C1=CC=C(C(Cl)=O)C=C1 LXEJRKJRKIFVNY-UHFFFAOYSA-N 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000005809 transesterification reaction Methods 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/03—Preparation of carboxylic acid esters by reacting an ester group with a hydroxy group
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
本发明涉及一种以新型催化剂催化醇解聚对苯二甲酸乙二醇酯(PET)制备对苯二甲酸二异辛酯(DOTP)的方法,其特点在于以胆碱类低共熔离子液体作为醇解的催化剂,催化剂合成时以氯化胆碱为氢键供体,金属盐为氢键受体。反应过程中以异辛醇作溶剂,在原料与溶剂摩尔比为1:2.5~1:8,反应温度为145℃~185℃,常压,反应时间为30min~180min,催化剂用量为原料质量的0.5%~10%的条件下进行醇解PET。该方法具有催化剂制备简单、成本低、反应条件温和、反应时间短、效率高、PET转化率高、目标产物选择性高且反应过程绿色环保等优点。The invention relates to a method for preparing diisooctyl terephthalate (DOTP) from polyethylene terephthalate (PET) catalyzed by a novel catalyst, which is characterized in that it uses choline deep eutectic ionic liquid As a catalyst for alcoholysis, when the catalyst is synthesized, choline chloride is used as a hydrogen bond donor, and metal salts are used as a hydrogen bond acceptor. In the reaction process, isooctanol is used as solvent, the molar ratio of raw material to solvent is 1:2.5~1:8, the reaction temperature is 145°C~185°C, normal pressure, the reaction time is 30min~180min, and the amount of catalyst used is the mass of raw material Carry out alcoholysis of PET under the condition of 0.5%~10%. The method has the advantages of simple catalyst preparation, low cost, mild reaction conditions, short reaction time, high efficiency, high PET conversion rate, high target product selectivity, and an environmentally friendly reaction process.
Description
技术领域technical field
本发明属于绿色、清洁催化技术领域,涉及一种新型催化剂催化醇解聚对苯二甲酸乙二醇酯(PET)制备对苯二甲酸二异辛酯的方法。The invention belongs to the technical field of green and clean catalysis, and relates to a method for preparing diisooctyl terephthalate by catalyzing alcohol decomposition of polyethylene terephthalate (PET) with a novel catalyst.
背景技术Background technique
对苯二甲酸二异辛酯(DOTP),又名对苯二甲酸二(2-乙基己),是近几年发展起来的新型增塑剂,应用于聚氯乙烯(PVC)塑料中的一种性能优良的主增塑剂,应用十分广泛。DOTP作为增塑剂使用的毒性低,安全性高,一直被公认为无毒的增塑剂,可以使用在医用PVC制品和塑料玩具中。Diisooctyl terephthalate (DOTP), also known as bis(2-ethylhexyl) terephthalate, is a new type of plasticizer developed in recent years and is used in polyvinyl chloride (PVC) plastics. A primary plasticizer with excellent performance, widely used. DOTP is used as a plasticizer with low toxicity and high safety. It has been recognized as a non-toxic plasticizer and can be used in medical PVC products and plastic toys.
到目前为止,工业上合成DOTP的方法主要有3种:一是对苯二甲酸与异辛醇直接酯化法;二是对苯二甲酸二甲酯酯交换法;三是聚对苯二甲酸乙二醇酯废料醇解法(PET法)。另外除此3种方法外,理论层面上还有对苯二甲酰氯法。采用前两种方法制备DOTP时对原料的要求较高,且反应过程较为复杂,反应成本高,所以聚对苯二甲酸乙二醇酯废料制备法(PET法)是目前研究最多的一种方法,因为聚酯工业生产中会产生很多废料,回收利用这些废料制备增塑剂不仅能够将废聚酯变废为宝,更能够给企业带来新的利润增长点,增加企业的效益。此工艺常规的催化剂为浓硫酸、氯化锌、钛酸四丁酯、氢氧化钠以及固体酸等。但这些催化剂存在着催化剂不稳定、腐蚀设备、催化剂活化时间过长导致反应缓慢以及反应所需温度较高等一系列问题。So far, there are three main methods for industrially synthesizing DOTP: one is the direct esterification of terephthalic acid and isooctyl alcohol; the other is the transesterification of dimethyl terephthalate; the third is polyterephthalic acid Ethylene glycol ester waste alcoholysis method (PET method). In addition to these three methods, there is also a terephthaloyl chloride method on a theoretical level. When using the first two methods to prepare DOTP, the requirements for raw materials are relatively high, and the reaction process is relatively complicated, and the reaction cost is high, so the polyethylene terephthalate waste preparation method (PET method) is currently the most studied method. , because there will be a lot of waste in the production of polyester industry, recycling these wastes to prepare plasticizers can not only turn waste polyester into treasure, but also bring new profit growth points to enterprises and increase the benefits of enterprises. The conventional catalysts for this process are concentrated sulfuric acid, zinc chloride, tetrabutyl titanate, sodium hydroxide and solid acid. However, these catalysts have a series of problems such as catalyst instability, corrosion of equipment, slow reaction due to long catalyst activation time, and high reaction temperature.
因为离子液体具有明显的绿色化学性质,所以将离子液体应用到某些催化反应之中,可以代替那些传统有毒、污染严重的非环保性催化剂。随着对离子液体研究的不断深入,研究者发现,当某些固体有机分子和特定的离子型化合物按一定比例混合时,可得到室温下呈液体状态的低共熔混合物,其中既含有离子成分,也含有一定数量的有机分子。这类低共熔离子液体不仅展示了与传统离子液体相似的物理化学性质,还具有容易制备、价格低廉、便于储存以及百分百的原子利用率等优势。由于自身所具备的优势,低共熔离子液体已经在许多研究领域引起了日渐增长的兴趣,关于低共熔离子液体作为便宜和安全的溶剂或催化剂用于许多催化过程的研究也越来越多。Because ionic liquids have obvious green chemical properties, the application of ionic liquids to certain catalytic reactions can replace those traditional toxic and heavily polluting non-environmentally friendly catalysts. With the deepening of research on ionic liquids, researchers have found that when some solid organic molecules and specific ionic compounds are mixed in a certain proportion, a eutectic mixture that is liquid at room temperature can be obtained, which contains both ionic components , also contains a certain amount of organic molecules. This kind of deep eutectic ionic liquid not only exhibits similar physical and chemical properties to traditional ionic liquids, but also has the advantages of easy preparation, low price, convenient storage, and 100% atom utilization. Due to their own advantages, deep eutectic ionic liquids have attracted increasing interest in many research fields, and there are more and more studies on deep eutectic ionic liquids as cheap and safe solvents or catalysts for many catalytic processes. .
将氯化胆碱和金属盐合成的低共熔催化剂用于降解PET制备 DOTP的反应中,催化剂显示出很高活性,与传统催化剂相比反应时间可减少5至8倍,且反应所需温度也有明显下降。两种原料之间以氢键或是金属的配位络合作用相结合,催化剂的高活性主要是因为胆碱与金属离子形成的协同作用,可同时进攻醇上的羟基和PET长链上的羰基,加速长链断开并与辛醇相连合成DOTP。该反应过程与传统反应过程相比具有条件温和、反应速率快、绿色环保等优点,为循环利用废旧PET制备环保增塑剂DOTP提供了一种高效可行的新方法。The eutectic catalyst synthesized by choline chloride and metal salt is used in the reaction of degrading PET to prepare DOTP. The catalyst shows high activity, and the reaction time can be reduced by 5 to 8 times compared with traditional catalysts, and the required temperature for the reaction There was also a marked decline. The two raw materials are combined by hydrogen bond or metal coordination and complexation. The high activity of the catalyst is mainly due to the synergistic effect formed by choline and metal ions, which can simultaneously attack the hydroxyl on the alcohol and the long chain of PET. The carbonyl group accelerates the breaking of the long chain and connects with octanol to synthesize DOTP. Compared with the traditional reaction process, the reaction process has the advantages of mild conditions, fast reaction rate, and environmental protection. It provides an efficient and feasible new method for recycling waste PET to prepare environmentally friendly plasticizer DOTP.
发明内容Contents of the invention
本发明研究以低共熔离子液体为催化剂、以异辛醇为溶剂,在温和的反应条件下,实现绿色节能、高效率、高转化率和高选择性的催化醇解PET制备对苯二甲酸二异辛酯(DOTP)的过程。The present invention uses deep eutectic ionic liquid as a catalyst and isooctanol as a solvent to realize green energy saving, high efficiency, high conversion rate and high selectivity to prepare terephthalic acid by catalytic alcoholysis of PET under mild reaction conditions Diisooctyl (DOTP) process.
本发明的反应通式为:General reaction formula of the present invention is:
以氯化胆碱和金属盐为原料合成的低共熔离子液体催化剂醇解聚对苯二甲酸乙二醇酯制备对苯二甲酸二异辛酯的方法,其特征在于以异辛醇为溶剂,以氯化胆碱与醋酸锌、氯化锌、硝酸锌、硫酸锌、醋酸锰、硝酸铜中的一种金属盐合成的低共熔离子液体催化剂醇解聚对苯二甲酸乙二醇酯制备对苯二甲酸二异辛酯。A method for preparing diisooctyl terephthalate by alcoholysis of polyethylene terephthalate with a deep eutectic ionic liquid catalyst synthesized from choline chloride and metal salts, characterized in that isooctanol is used as a solvent , a deep eutectic ionic liquid catalyst synthesized with choline chloride and a metal salt of zinc acetate, zinc chloride, zinc nitrate, zinc sulfate, manganese acetate, and copper nitrate for alcoholysis of polyethylene terephthalate Preparation of di-isooctyl terephthalate.
所降解的聚对苯二甲酸乙二醇酯原料来源为矿泉水瓶、碳酸饮料瓶和茶饮料瓶中的一种或几种的混合物或聚对苯二甲酸乙二醇酯颗粒。The raw material source of the degraded polyethylene terephthalate is one or a mixture of mineral water bottles, carbonated beverage bottles and tea beverage bottles or polyethylene terephthalate particles.
所述以氯化胆碱与醋酸锌、氯化锌、硝酸锌、硫酸锌、醋酸锰、硝酸铜为原料合成低共熔离子液体时,氯化胆碱与金属盐的摩尔比为 1:0.1~1:2。When using choline chloride and zinc acetate, zinc chloride, zinc nitrate, zinc sulfate, manganese acetate, copper nitrate as raw materials to synthesize eutectic ionic liquid, the molar ratio of choline chloride and metal salt is 1:0.1 ~1:2.
所述以氯化胆碱与醋酸锌、氯化锌、硝酸锌、硫酸锌、醋酸锰、硝酸铜为原料合成低共熔离子液体时,其反应温度为50℃~120℃,反应时间为30min~240min。When using choline chloride, zinc acetate, zinc chloride, zinc nitrate, zinc sulfate, manganese acetate, and copper nitrate as raw materials to synthesize the eutectic ionic liquid, the reaction temperature is 50°C to 120°C, and the reaction time is 30min ~240min.
所述催化剂用量为聚对苯二甲酸乙二醇酯质量的0.5%~10%。The dosage of the catalyst is 0.5%-10% of the mass of polyethylene terephthalate.
所述以胆碱类低共熔离子液体作催化剂降解聚对苯二甲酸乙二醇酯制备对苯二甲酸二异辛酯的原料与溶剂摩尔比为1:2.5~1:8。The molar ratio of raw material to solvent for preparing di-isooctyl terephthalate by using choline deep eutectic ionic liquid as a catalyst to degrade polyethylene terephthalate is 1:2.5-1:8.
所述以胆碱类低共熔离子液体作催化剂降解聚对苯二甲酸乙二醇酯制备对苯二甲酸二异辛酯的反应温度为145℃~185℃。The reaction temperature for preparing di-isooctyl terephthalate by using choline deep eutectic ionic liquid as a catalyst to degrade polyethylene terephthalate is 145° C. to 185° C.
所述以胆碱类低共熔离子液体作催化剂降解聚对苯二甲酸乙二醇酯制备对苯二甲酸二异辛酯的反应时间为30min~180min。The reaction time for preparing diisooctyl terephthalate by using choline deep eutectic ionic liquid as a catalyst to degrade polyethylene terephthalate is 30 minutes to 180 minutes.
反应结束后,PET的降解率和产物的选择性分别按公式(1)(2) 计算:After the reaction finishes, the degradation rate of PET and the selectivity of product are calculated by formula (1) (2) respectively:
其中,A表示加入的PET的初始质量,B表示反应结束后未降解PET的质量。Among them, A represents the initial mass of PET added, and B represents the mass of undegraded PET after the reaction.
具体实施方案specific implementation plan
本发明用以下实施例进行说明,但本发明并不仅限于下述实施例,在不脱离前后所属宗旨的范围下,变化实施都包含在本发明的技术范围内。The present invention is described with the following examples, but the present invention is not limited to the following examples, and all changes are included in the technical scope of the present invention without departing from the scope of the subject.
实施例1Example 1
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锌,两者摩尔比为1:2,合成条件为 70℃,120min。控制反应温度为175℃,常压,冷凝回流反应60min 后冷却至室温。在此条件下,PET的降解率为100%,对苯二甲酸二异辛酯(DOTP)的选择性为78.2%。Using PET granules as raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.25g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-necked round-bottomed flask. The raw materials for the synthesis catalyst were choline chloride and zinc acetate. The molar ratio is 1:2, and the synthesis conditions are 70°C, 120min. The reaction temperature was controlled at 175° C. under normal pressure, condensed and refluxed for 60 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 100%, and the selectivity of di-isooctyl terephthalate (DOTP) is 78.2%.
实施例2Example 2
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锌,两者摩尔比为1:1.5,合成条件为 70℃,120min。控制反应温度为185℃,常压,冷凝回流反应60min后冷却至室温。在此条件下,PET的降解率为100%,对苯二甲酸二异辛酯(DOTP)的选择性为82.5%。Using PET granules as raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.25g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-necked round-bottomed flask. The raw materials for the synthesis catalyst were choline chloride and zinc acetate. The molar ratio is 1:1.5, and the synthesis conditions are 70°C, 120min. The reaction temperature was controlled at 185° C. under normal pressure, condensed and refluxed for 60 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 100%, and the selectivity of di-isooctyl terephthalate (DOTP) is 82.5%.
实施例3Example 3
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锌,两者摩尔比为1:0.25,合成条件为 50℃,240min。控制反应温度为185℃,常压,冷凝回流反应60min后冷却至室温。在此条件下,PET的降解率为99.2%,对苯二甲酸二异辛酯(DOTP)的选择性为79.4%。Using PET granules as raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.25g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-necked round-bottomed flask. The raw materials for the synthesis catalyst were choline chloride and zinc acetate. The molar ratio is 1:0.25, and the synthesis conditions are 50°C, 240min. The reaction temperature was controlled at 185° C. under normal pressure, condensed and refluxed for 60 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 99.2%, and the selectivity of di-isooctyl terephthalate (DOTP) is 79.4%.
实施例4Example 4
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锌,两者摩尔比为1:2,合成条件为90℃,180min。控制反应温度为175℃,常压,冷凝回流反应60min 后冷却至室温。在此条件下,PET的降解率为100%,对苯二甲酸二异辛酯(DOTP)的选择性为78.4%。Using PET granules as raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.25g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-necked round-bottomed flask. The raw materials for the synthesis catalyst were choline chloride and zinc acetate. The molar ratio is 1:2, and the synthesis conditions are 90°C, 180min. The reaction temperature was controlled at 175° C. under normal pressure, condensed and refluxed for 60 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 100%, and the selectivity of di-isooctyl terephthalate (DOTP) is 78.4%.
实施例5Example 5
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锌,两者摩尔比为1:0.25,合成条件为 70℃,120min。控制反应温度为175℃,常压,冷凝回流反应120min后冷却至室温。在此条件下,PET的降解率为100%,对苯二甲酸二异辛酯(DOTP)的选择性为75.3%。Using PET granules as raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.25g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-necked round-bottomed flask. The raw materials for the synthesis catalyst were choline chloride and zinc acetate. The molar ratio is 1:0.25, and the synthesis conditions are 70°C, 120min. The reaction temperature was controlled at 175° C. under normal pressure, condensed and refluxed for 120 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 100%, and the selectivity of di-isooctyl terephthalate (DOTP) is 75.3%.
实施例6Example 6
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锌,两者摩尔比为1:0.1,合成条件为 70℃,120min。控制反应温度为175℃,常压,冷凝回流反应120min后冷却至室温。在此条件下,PET的降解率为98.7%,对苯二甲酸二异辛酯(DOTP)的选择性为79.4%。Using PET granules as raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.25g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-necked round-bottomed flask. The raw materials for the synthesis catalyst were choline chloride and zinc acetate. The molar ratio is 1:0.1, and the synthesis conditions are 70°C, 120min. The reaction temperature was controlled at 175° C. under normal pressure, condensed and refluxed for 120 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 98.7%, and the selectivity of di-isooctyl terephthalate (DOTP) is 79.4%.
实施例7Example 7
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锌,两者摩尔比为1:1,合成条件为 85℃,120min。控制反应温度为155℃,常压,冷凝回流反应120min 后冷却至室温。在此条件下,PET的降解率为88.3%,对苯二甲酸二异辛酯(DOTP)的选择性为93.4%。Using PET granules as raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.25g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-necked round-bottomed flask. The raw materials for the synthesis catalyst were choline chloride and zinc acetate. The molar ratio is 1:1, and the synthesis conditions are 85°C, 120min. The reaction temperature was controlled at 155° C. under normal pressure, condensed and refluxed for 120 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 88.3%, and the selectivity of di-isooctyl terephthalate (DOTP) is 93.4%.
实施例8Example 8
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锌,两者摩尔比为1:1,合成条件为 100℃,90min。控制反应温度为145℃,常压,冷凝回流反应180min 后冷却至室温。在此条件下,PET的降解率为83.9%,对苯二甲酸二异辛酯(DOTP)的选择性为94.6%。Using PET granules as raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.25g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-necked round-bottomed flask. The raw materials for the synthesis catalyst were choline chloride and zinc acetate. The molar ratio is 1:1, and the synthesis conditions are 100°C, 90min. The reaction temperature was controlled at 145° C. under normal pressure, condensed and refluxed for 180 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 83.9%, and the selectivity of di-isooctyl terephthalate (DOTP) is 94.6%.
实施例9Example 9
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锌,两者摩尔比为1:1,合成条件为 80℃,120min。控制反应温度为185℃,常压,冷凝回流反应180min 后冷却至室温。在此条件下,PET的降解率为100%,对苯二甲酸二异辛酯(DOTP)的选择性为84.5%。Using PET granules as raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.25g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-necked round-bottomed flask. The raw materials for the synthesis catalyst were choline chloride and zinc acetate. The molar ratio is 1:1, and the synthesis conditions are 80°C, 120min. The reaction temperature was controlled at 185° C. under normal pressure, condensed and refluxed for 180 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 100%, and the selectivity of di-isooctyl terephthalate (DOTP) is 84.5%.
实施例10Example 10
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锌,两者摩尔比为1:1,合成条件为 120℃,60min。控制反应温度为145℃,常压,冷凝回流反应180min 后冷却至室温。在此条件下,PET的降解率为93.9%,对苯二甲酸二异辛酯(DOTP)的选择性为94.6%。Using PET granules as raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.25g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-necked round-bottomed flask. The raw materials for the synthesis catalyst were choline chloride and zinc acetate. The molar ratio is 1:1, and the synthesis conditions are 120°C, 60min. The reaction temperature was controlled at 145° C. under normal pressure, condensed and refluxed for 180 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 93.9%, and the selectivity of di-isooctyl terephthalate (DOTP) is 94.6%.
实施例11Example 11
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、27.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锌,两者摩尔比为1:1,合成条件为 120℃,30min。控制反应温度为155℃,常压,冷凝回流反应180min 后冷却至室温。在此条件下,PET的降解率为95.9%,对苯二甲酸二异辛酯(DOTP)的选择性为95.7%。Using PET particles as raw materials, 5.0g PET raw materials, 27.0g isooctyl alcohol and 0.25g choline-based eutectic ionic liquid catalyst were added successively in a 50ml three-necked round-bottomed flask. The raw materials for the synthesis catalyst were choline chloride and zinc acetate. The molar ratio is 1:1, and the synthesis conditions are 120°C, 30min. The reaction temperature was controlled at 155° C. under normal pressure, condensed and refluxed for 180 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 95.9%, and the selectivity of di-isooctyl terephthalate (DOTP) is 95.7%.
实施例12Example 12
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、12.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锌,两者摩尔比为1:2,合成条件为 70℃,120min。控制反应温度为145℃,常压,冷凝回流反应180min 后冷却至室温。在此条件下,PET的降解率为97.9%,对苯二甲酸二异辛酯(DOTP)的选择性为94.4%。Using PET granules as raw material, 5.0g PET raw material, 12.0g isooctyl alcohol and 0.25g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-neck round bottom flask. The raw materials of the synthetic catalyst were choline chloride and zinc acetate, two The molar ratio is 1:2, and the synthesis conditions are 70°C, 120min. The reaction temperature was controlled at 145° C. under normal pressure, condensed and refluxed for 180 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 97.9%, and the selectivity of di-isooctyl terephthalate (DOTP) is 94.4%.
实施例13Example 13
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和硝酸铜,两者摩尔比为1:1,合成条件为 70℃,120min。控制反应温度为185℃,常压,冷凝回流反应120min 后冷却至室温。在此条件下,PET的降解率为100%,对苯二甲酸二异辛酯(DOTP)的选择性为78.4%。Using PET particles as raw materials, 5.0g PET raw materials, 17.0g isooctyl alcohol and 0.25g choline-based eutectic ionic liquid catalyst were successively added in a 50ml three-necked round-bottomed flask. The raw materials for the synthesis catalyst were choline chloride and copper nitrate. The molar ratio is 1:1, and the synthesis conditions are 70°C, 120min. The reaction temperature was controlled at 185° C. under normal pressure, condensed and refluxed for 120 minutes and then cooled to room temperature. Under these conditions, the degradation rate of PET is 100%, and the selectivity of di-isooctyl terephthalate (DOTP) is 78.4%.
实施例14Example 14
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锰,两者摩尔比为1:1,合成条件为 70℃,120min。控制反应温度为185℃,常压,冷凝回流反应120min 后冷却至室温。在此条件下,PET的降解率为100%,对苯二甲酸二异辛酯(DOTP)的选择性为79.2%。Using PET granules as raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.25g choline-based eutectic ionic liquid catalyst were added successively in a 50ml three-necked round-bottomed flask. The raw materials for the synthesis catalyst were choline chloride and manganese acetate, two The molar ratio is 1:1, and the synthesis conditions are 70°C, 120min. The reaction temperature was controlled at 185° C. under normal pressure, condensed and refluxed for 120 minutes and then cooled to room temperature. Under these conditions, the degradation rate of PET is 100%, and the selectivity of di-isooctyl terephthalate (DOTP) is 79.2%.
实施例15Example 15
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和硫酸锌,两者摩尔比为1:1,合成条件为 70℃,120min。控制反应温度为185℃,常压,冷凝回流反应120min 后冷却至室温。在此条件下,PET的降解率为100%,对苯二甲酸二异辛酯(DOTP)的选择性为78.9%。Using PET granules as raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.25g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-neck round bottom flask. The raw materials for the synthesis catalyst were choline chloride and zinc sulfate. The molar ratio is 1:1, and the synthesis conditions are 70°C, 120min. The reaction temperature was controlled at 185° C. under normal pressure, condensed and refluxed for 120 minutes and then cooled to room temperature. Under these conditions, the degradation rate of PET is 100%, and the selectivity of di-isooctyl terephthalate (DOTP) is 78.9%.
实施例16Example 16
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.5g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锌,两者摩尔比为1:1,合成条件为60℃, 180min。控制反应温度为175℃,常压,冷凝回流反应30min后冷却至室温。在此条件下,PET的降解率为97.5%,对苯二甲酸二异辛酯 (DOTP)的选择性为84.7%。Using PET granules as raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.5g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-neck round bottom flask. The raw materials for the synthesis catalyst were choline chloride and zinc acetate. The molar ratio is 1:1, and the synthesis conditions are 60° C., 180 min. The reaction temperature was controlled at 175° C. under normal pressure, condensed and refluxed for 30 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 97.5%, and the selectivity of di-isooctyl terephthalate (DOTP) is 84.7%.
实施例17Example 17
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和氯化锌,两者摩尔比为1:1,合成条件为 70℃,120min。控制反应温度为185℃,常压,冷凝回流反应120min 后冷却至室温。在此条件下,PET的降解率为100%,对苯二甲酸二异辛酯(DOTP)的选择性为82.8%。Using PET granules as raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.25g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-neck round bottom flask, and the raw materials of the synthetic catalyst were choline chloride and zinc chloride, The molar ratio of the two is 1:1, and the synthesis conditions are 70°C, 120min. The reaction temperature was controlled at 185° C. under normal pressure, condensed and refluxed for 120 minutes and then cooled to room temperature. Under these conditions, the degradation rate of PET is 100%, and the selectivity of di-isooctyl terephthalate (DOTP) is 82.8%.
实施例18Example 18
以边长为0.5cm×0.5cm的雪碧瓶片为PET原料,在50ml三口圆底烧瓶中依次加入5.0gPET原料、17.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和氯化锌,两者摩尔比为1:1,合成条件为80℃,120min。控制反应温度为185℃,常压,冷凝回流反应120min后冷却至室温。在此条件下,PET的降解率为100%,对苯二甲酸二异辛酯(DOTP)的选择性为80.6%。With the Sprite bottle flakes with a side length of 0.5cm × 0.5cm as the PET raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.25g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-neck round bottom flask to synthesize the catalyst. The raw materials are choline chloride and zinc chloride, the molar ratio of the two is 1:1, and the synthesis conditions are 80°C, 120min. The reaction temperature was controlled at 185° C. under normal pressure, condensed and refluxed for 120 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 100%, and the selectivity of di-isooctyl terephthalate (DOTP) is 80.6%.
实施例19Example 19
以边长为0.5cm×0.5cm的矿泉水瓶片为PET原料,在50ml三口圆底烧瓶中依次加入5.0gPET原料、17.0g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和硝酸锌,两者摩尔比为1:1,合成条件为70℃,120min。控制反应温度为185℃,常压,冷凝回流反应120min后冷却至室温。在此条件下,PET的降解率为100%,对苯二甲酸二异辛酯(DOTP)的选择性为79.4%。With the side length of 0.5cm × 0.5cm mineral water bottle flakes as PET raw materials, 5.0g PET raw materials, 17.0g isooctyl alcohol and 0.25g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-neck round bottom flask, and the catalyst was synthesized. The raw materials are choline chloride and zinc nitrate, the molar ratio of the two is 1:1, and the synthesis conditions are 70°C, 120min. The reaction temperature was controlled at 185° C. under normal pressure, condensed and refluxed for 120 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 100%, and the selectivity of di-isooctyl terephthalate (DOTP) is 79.4%.
实施例20Example 20
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.5g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锌,两者摩尔比为1:1,合成条件为70℃, 120min。控制反应温度为185℃,常压,冷凝回流反应60min后冷却至室温。在此条件下,PET的降解率为100%,对苯二甲酸二异辛酯 (DOTP)的选择性为83.5%。Using PET granules as raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.5g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-neck round bottom flask. The raw materials for the synthesis catalyst were choline chloride and zinc acetate. The molar ratio is 1:1, and the synthesis conditions are 70°C, 120min. The reaction temperature was controlled at 185° C. under normal pressure, condensed and refluxed for 60 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 100%, and the selectivity of di-isooctyl terephthalate (DOTP) is 83.5%.
实施例21Example 21
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、8.5g异辛醇和0.25g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锌,两者摩尔比为1:2,合成条件为70℃, 120min。控制反应温度为185℃,常压,冷凝回流反应60min后冷却至室温。在此条件下,PET的降解率为97.5%,对苯二甲酸二异辛酯 (DOTP)的选择性为74.4%。Using PET granules as raw material, 5.0g PET raw material, 8.5g isooctyl alcohol and 0.25g choline deep eutectic ionic liquid catalyst were added successively in a 50ml three-neck round bottom flask. The raw materials of the synthetic catalyst were choline chloride and zinc acetate. The molar ratio is 1:2, and the synthesis conditions are 70°C, 120min. The reaction temperature was controlled at 185° C. under normal pressure, condensed and refluxed for 60 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 97.5%, and the selectivity of di-isooctyl terephthalate (DOTP) is 74.4%.
实施例22Example 22
以PET颗粒为原料,在50ml三口圆底烧瓶中依次加入5.0gPET 原料、17.0g异辛醇和0.025g胆碱类低共熔离子液体催化剂,合成催化剂的原料为氯化胆碱和醋酸锌,两者摩尔比为1:2,合成条件为 70℃,120min。控制反应温度为185℃,常压,冷凝回流反应120min后冷却至室温。在此条件下,PET的降解率为99.5%,对苯二甲酸二异辛酯(DOTP)的选择性为77.6%。Using PET granules as raw material, 5.0g PET raw material, 17.0g isooctyl alcohol and 0.025g choline-based eutectic ionic liquid catalyst were added successively in a 50ml three-necked round-bottomed flask. The raw materials for the synthesis catalyst were choline chloride and zinc acetate. The molar ratio is 1:2, and the synthesis conditions are 70°C, 120min. The reaction temperature was controlled at 185° C. under normal pressure, condensed and refluxed for 120 minutes, and then cooled to room temperature. Under these conditions, the degradation rate of PET is 99.5%, and the selectivity of di-isooctyl terephthalate (DOTP) is 77.6%.
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