用废聚对苯二甲酸乙二醇酯制备对苯型不饱和聚酯树脂

用废聚对苯二甲酸乙二醇酯(PET)制备对苯型不饱和聚酯树脂。考察了醇解时间对醇解产物、聚合温度对反应产物的影响。该方法的主要工艺参数为：废PET：PG(摩尔比)等于1：1．5,废PET：MA(摩尔比)等于1：1,醇解温度190～200℃,醇解时间3．5～4h,聚合温度190～210℃,聚合反应时间1．5～2h。试验所得对苯型不饱和聚酯树脂产品的性能符合企业通用型不饱和聚酯树脂的标准。     

用废聚酯塑料制品生产1730聚酯绝缘漆

1730聚酯绝缘漆最早由西德 Beck公司研制成功 ,并用于 B级漆包线 (使用温度低于 1 30℃ ) ,现已有 5 0多年的使用历史。我国于 1 962年后将 B级绝缘材料大量用于机电工业 ,至今仍在使用。目前 ,国内外普遍以对苯二甲酸二甲酯单体为原料 ,经过与多元醇醇解、缩聚的工艺路线生产 1 730聚酯绝缘漆。我们以废聚酯塑料制品 (主要是废弃的矿泉水瓶 ,其化学成分是聚对苯二甲酸乙二醇酯 )为原料 ,经醇解、解聚一步完成 ,然后进行缩聚等工艺制得1 730聚酯绝缘漆。研究了原料配比、醇解温度和反应时间、缩聚反应温度、真空度等工艺参数对产品质量的…     

废聚酯用品回收技术获成功

日本帝人公司研制成功从废聚酯用品回收高纯度对苯二甲酸二甲酯(DMT)和乙二醇(EG)的化学回收技术。 该技术可回收利用与其他材料混合的制成品或使用了添加剂、加工剂的制成品,得到的产品与未用过的DMT、EG产品纯度相同。 据报道,该公司目前正在改造其德山事业所的旧DMT设备,以建成年生产能力为3万吨的回收专用设备。预计这些设备可在2002年度投产。 帝人公司称,它目前主要以聚对苯二甲酸乙二醇酯)PET)瓶为回收对象,并将继续考虑利用聚酯纤维、聚酯薄膜等,公司用该技术回收的DMT等将全部自用消化。 据介绍,这项技术是将使用后的聚酯瓶粉碎、洗净,经解聚工序分离工序后,进入酯交换和重结晶工序、DMT分离工序及精制工序,精制后的DMT再经反应,得到高纯度对苯二甲酸(PTA),再生DMT纯度达99.99%,与未曾用过的纯品质量相同。 (汪硕)     

聚对苯二甲酸乙二醇酯废料的回收方法

介绍了聚对苯二甲酸乙二醇酯传统的化学回收方法：甲醇醇解法、水解法和醣酵解法;简述了聚酯新的回收工艺：伊斯曼乙二醇水解工艺、超临界水水解工艺和Reco-PET工艺,及有关国家聚酯回收的工业化实践,并对聚酯回收的前景及影响聚酯回收的因素进行了分析。     

乙二醇降解聚2,6-萘二甲酸乙二醇酯

采用乙二醇对聚2,6-萘二甲酸乙二醇酯（PEN）进行降解,表征了醇解产物,探讨了醇解原理。结果表明：醇解后PEN中的酯键断裂,PEN分子内的蟄合羟基变成2,6-萘二甲酸乙二醇酯（BHEN）上分子间缔合羟基和游离羟基;醇解后产物的O与C的原子比由醇解前的0.28增至0.38,醇解产物中C=O和C—O两种O结构的质量比为1∶2.18,C—C、C—O和O—C=O三种C结构的质量比为5.38∶2.22∶1,产物的平均分子量降为200左右;醇解产物主要为BHEN及其低聚物,BHEN单体纯度在90%以上,收率为25.95%。该醇解反应是酯基断裂又聚合,PEN长链变短的过程。     

镁-铝水滑石的制备及其脱色性能

以不同的Mg^2＋与Al^3＋摩尔比制备一系列的镁-铝水滑石，考察镁-铝水滑石对单一品种模拟分散染料废水的脱色效果。实验结果表明，以n（Mg^2＋）：n（Al^3＋）为3：1制得的镁-铝水滑石对模拟分散染料废水的脱色效果最好；脱色处理后的镁-铝水滑石再生后可重复使用，它对模拟分散染料废水的脱色效果与新的镁-铝水滑石的脱色效果几乎没有差别；在模拟分散染料废水pH为10～11、镁-铝水滑石的加入量为1.0g／L、反应2h的条件F，模拟分散染料废水的脱色率为98％。     

氧化亚氮分解催化剂的研究进展

对近年来N2O分解反应催化剂的研究进行了综述,包括离子交换分子筛、过渡金属氧化物、负载型贵金属等催化剂.对于离子交换分子筛催化剂而言,分子筛骨架结构、交换离子类型、制备方法均对催化剂的活性有一定影响.在过渡金属氧化物催化剂中,Co-A1、Co-Mn-A1等类水滑石衍生复合氧化物的比表面积和催化活性均较高,在其表面添加适量的碱金属或碱土金属助剂可进一步提高催化活性.在贵金属催化剂中,还原型载体负载的催化剂活性较高.Co基复合氧化物负载Au催化剂有望成为实用型的N2O低温分解催化剂.     

用含锌废催化剂制备纳米氧化锌

以含锌废催化剂为原料,经酸浸、除杂、锌粉置换、合成等工艺制得碱式碳酸锌,再经过滤、洗涤、干燥、煅烧制备纳米氧化锌。考察了酸浸工艺硫酸溶液含量和液固比(硫酸与含锌废催化剂的质量比)对锌浸出率的影响,以及煅烧温度对纳米氧化锌质量的影响。实验结果表明:在硫酸质量分数为30%、液固比为5的最佳酸浸工艺条件下,锌浸出率为92%;在最佳煅烧温度为400℃的条件下,氧化锌质量分数大于95%,比表面积大于50 m2/g;纳米氧化锌颗粒大小均匀,平均粒径小于50 nm。     

催化燃烧法处理聚对苯二甲酸乙二醇酯生产废气

采用催化燃烧法处理聚对苯二甲酸乙二醇酯生产过程排放的含乙醛、2-甲基-1，3-二氧戊烷、乙二醇的废气，用进口Pt Pd／Al2O3-CeO2球状催化剂作废气催化燃烧的催化剂。在催化燃烧反应器床层空速为20000h^-1、催化剂用量为935mL、反应器入口温度为250℃、进口废气总烃质量浓度为2555～5099mg／m^3的条件下，处理后废气的总烃质量浓度为1～38mg／m^3，远低于120mg/m^3的国家排放标准，且总烃去除率达到98．6％～100％，乙醛质量浓度小于99mg／m^3,低于125mg／m^3的国家排放标准。     

土壤残留塑料的热降解脱附研究

针对土壤的塑料污染问题,提出一种采用热脱附降解技术修复污染土壤的方法。选取4种土壤中常见的残留塑料（聚乙烯（PE）、聚氯乙烯（PVC）、聚对苯二甲酸乙二酯（PET）、聚丙烯（PP））为研究对象,通过控制热解温度和土壤含水率对各污染土壤的修复效果进行探究。实验结果表明：在500 ℃的最佳热解温度下处理60 min,PE、PVC、PET和PP的去除率分别达到92.61%、91.73%、90.74%和93.42%;土壤含水率低于16%时对修复效果的影响不显著。表征结果显示,500 ℃热解后土壤中残留有机成分已得到充分挥发,热解油的主要组分为烷烃。     

Chemical Recycling of PET Waste with Multifunctional Pentaerythrytol in the Melt State

Chemical recycling of poly(ethylene terephthalate) PET waste in the melt state through alcoholysis with multifunctional alcohol—pentaerythrytol (PENTE)—was performed in a internal mixer Haake Rheomix 600, at 250 °C, 60 rpm, for 10 min, in presence of zinc acetate. The following PET:PENTE molar ratios 1:0; 1:0.16; 1:0.48 and 1:3.4 were studied. The chemical structure of the end-products was characterized by FT-IR. Thermal properties and X-ray diffractograms were also assessed. The esterification and alcoholysis reactions took place and were dependent on the molar ratio. The first one is dominant in compositions rich in PET leading to the formation of star-branching copolymer. The second one brings about the PET oligomerization and an oligoester named herein bis(tri-hydroxylneopentyl) terephthalate (BTHNPT) was obtained. The end-products have potential application as asphalt additive or adhesive.     

Decomposition of mixed plastics consisting of polypropylene and polyethylene terephthalate into oils over titania/silica catalysts

The catalytic decomposition of mixed plastics consisting of polypropylene (PP) and polyethylene terephthalate (PET) has been investigated over titania/silica catalysts at 698 K. The yield of oil produced was about 70%, and the large amounts of C₁₈₊ hydrocarbons this contained was from the aromatics in PET. Gas was also produced, including C₃–C₅ hydrocarbons. The carbon-number fractions in the oil was influenced by the PET/(PP + PET) ratios and the catalyst weight. The titania/silica catalysts could be used repeatedly, and after they had been fouled, could be regenerated. From the Fourier Transform Infrared (FT–IR) spectroscopic data of adsorbed pyridine on the catalyst surface, most of the acid sites of the titania/silica catalysts were found to be Lewis sites where the hydride abstracted from PP pyrolysates react with PET pyrolysates to form oil and gas. Received: July 19, 2000 / Accepted: October 20, 2000     

Recovery of benzene-rich oil from the degradation of metal- and metal oxide-containing poly(ethylene terephthalate) composites

Pure poly(ethylene terephthalate) (PET) resin and metal-/metal oxide-containing PET composites were thermally decomposed in the presence of Ca(OH)₂ using a tube reactor. The effects of batch and continuous processing, the presence of Ca(OH)₂, and PET size on benzene production were investigated. A maximum benzene yield and purity of 82.9 % and 78.8 wt%, respectively, were obtained at 700 °C in the presence of Ca(OH)₂ when using small PET particles; further, a continuous feed reactor was favored over a batch reactor. Effective contact between PET and Ca(OH)₂ was important in the PET degradation, which promoted hydrolysis of PET and decarboxylation of terephthalic acid, whereas pyrolysis was suppressed. Furthermore, the results of thermal decomposition of PET-based waste—PET-based X-ray films, magnetic tape, and prepaid cards—indicated that the metal and metal oxides contained in the waste had no significant catalytic effect on PET degradation or on the recovery of benzene-rich oil in the presence of Ca(OH)₂.     

Recycling of waste PET into useful textile auxiliaries

Polyethylene terephthalate (PET) waste fibers were initially depolymerized using a glycolysis route in the presence of sodium sulfate as a catalyst, which is a commonly used chemical and ecofriendly as compared to heavy metal catalysts. Good yield of the pure monomer bis(2-hydroxyethylene terephthalate) (BHET) was obtained. Further, to attempt its reuse, the purified BHET was converted to different fatty amide derivatives to obtain quaternary ammonium compounds that have a potential for use as softener in the textile finishing process. The products were characterized by infrared spectroscopy. Application of these synthesized compounds was carried out on cotton fabric; they were evaluated for performance and were found to give good results. The chemicals used during depolymerization and reuse of PET are inexpensive and comparatively less harmful to the environment, and thus offer advantages in the chemical recycling of polyester waste fibers.     

Catalytic upgrading pyrolysis of pine sawdust for bio-oil with metal oxides

The catalytic upgrading pyrolysis of pine sawdust was performed at 500 °C with various metal oxides to improve the quality of the bio-oil. The aim of this study was to investigate the potential of the metal oxides instead of traditional zeolites for catalytic upgrading pyrolysis with the analysis of Gas Chromatograph/Mass Spectrometer. In this study, the used catalysts were Calcium-oxide, Magnesium oxide, Titanium dioxide, and Zeolite (Si/Al?=?80). The influence of catalysts on products yields and compositions were investigated. Most metal oxides can enhance the bio-gas with the bio-oil yields decreased. The metal oxides led to a decrease of Acids, Aldehydes, Ketones and an increase of Furfural, Cresols, Catechols in Furans and Phenolics. Among the catalysts, the MgO catalysts was the most effective to convert the high molecular into lights ones (6.65% Cresols) with yield of 20.48% for Furfural. The deoxygenation reaction in bio-oil was suggested to convert oxygenated compounds into the low molecular weight of the materials (6.39% Guaiacols). Thus, the used metal oxides can improve the quality of bio-oil by decreasing undesirable compounds as well as increasing the desirable compounds with low oxygen contents via deoxygenation reaction.     

One-Pot Reaction of Waste PET to Flame Retardant Polyurethane Foam,via Deep Eutectic Solvents-Based Conversion Technology

Depolymerization of polyethylene terephthalate (PET) is a promising technology for producing recycled monomers. Using a deep eutectic solvent (DES)-based catalyst, the PET glycolysis process produces bis-(2-hydroxyethylene terephthalate) (BHET). This recycled monomer reacts with isocyanate and forms polyurethane foam (PUF). The DES-based one-pot reaction is advantageous because it is a low-energy process that requires relatively lower temperatures and reduced reaction times. In this study, choline chloride/urea, zinc chloride/urea, and zinc acetate/urea based DESs were adopted as DES catalysts for glycolysis. Subsequently, the conversion of PET, BHET yield, and OH values were evaluated. Both filtered and unfiltered reaction mixtures were used as polyols for PUF polymerization after characterization of the acid and hydroxyl values of the polyols, as well as the NCO (–N=C=O) value of isocyanate. In the case of unfiltered reaction mixtures, PUF was obtained via a one-pot reaction, which exhibited higher thermal stability than PUF made from the filtered polyols. This outcome indicated that oligomeric BHET containing many aromatic moieties in unfiltered polyols contributes to the thermal stability of PUF. This environmentally friendly and relatively simple process is an economical approach for upcycling waste PET.

     

Chemical depolymerisation of PET complex waste: hydrolysis vs. glycolysis

The huge increase in the generation of post-consumer plastic waste has produced a growing interest in eco-efficient strategies and technologies for their appropriate management and recycling. In response to this, PROQUIPOL Project is focused on developing, optimizing and adapting feedstock recycling technologies as an alternative for management for the treatment of complex plastic waste. Among the different plastic wastes studied, PROQUIPOL Project is working on providing a suitable treatment to the highly colored and complex multilayered post-consumer waste fractions of polyethylene terephthalate (PET) by chemical depolymerisation methods. Glycolysis and alkali hydrolysis processes have been studied with the aim of promoting the transformation of PET into the bis(2-hydroxyethyl) terephthalate monomer and terephthalic acid, respectively. In both cases operational conditions such as temperature, reaction time, catalyst to PET rate and solvent to PET rate have been considered to optimize product yield, achieving values near to 90 % and monomer purities over 95 % in both processes. This paper presents results obtained for each treatment as well as a simplified comparison of technical, economic and environmental issues.     

Modification of Thermo-Mechanical Properties of Recycled PET by Vinyl Acetate (VAc) Monomer Grafting Using Gamma Irradiation

Vinyl acetate (VAc) monomer of different percentage was grafted onto the recycled polyethylene terephthalate (r-PET) films using gamma irradiation. The properties of these modified films were characterized by Fourier transform infrared spectroscopy (FTIR), mechanical properties testing (Tensile strength, Elongation at break), dynamic mechanical analysis (DMA) and thermo-gravimetric analysis (TGA). The Tensile Strength (TS) of the modified PET film increased by 132.25?% to the highest value of 50.12 MPa at 15% VAc monomer concentration at 3 kGy gamma dose, while the elongation at break (EB) decreased by 31.83?%. FTIR was used to investigate the molecular interaction of the modified films. TGA revealed that curve of the modified PET film shifted toward higher temperature region by 95?°C, which is very close to that of PET film made from virgin flakes. The results indicate that modified PET films of better mechanical and thermal properties were successfully prepared using VAc monomer grafting by gamma irradiation technique.     

低温NH_3-SCR脱硝催化剂的研究现状与进展

高效催化剂的研制与开发是低温氨气选择性催化还原(NH_3-SCR)脱硝技术的核心。从活性组分(单一氧化物型、复合氧化物型)和载体(金属氧化物、碳基材料、分子筛)两方面详细介绍了低温NH_3-SCR催化剂,总结了其研究现状,并讨论了其抗水、抗硫性能及失活原因。指出在保证催化剂具有较高活性的同时提高其抗水、抗硫性能,是低温NH_3-SCR催化剂未来研究的重点。