首页> 外国专利> NEW PROCEDURE FOR PRODUCTION OF REGRANULATES FROM POLYVINYL CHLORIDE (PVC) AND DIOCTYL TEREPHTHALATE FOR APPLICATION IN CIVIL ENGINEERING, INDUSTRY AND FOR MANUFACTURE OF OBJECTS FOR GENERAL USE

NEW PROCEDURE FOR PRODUCTION OF REGRANULATES FROM POLYVINYL CHLORIDE (PVC) AND DIOCTYL TEREPHTHALATE FOR APPLICATION IN CIVIL ENGINEERING, INDUSTRY AND FOR MANUFACTURE OF OBJECTS FOR GENERAL USE

机译:由聚氯乙烯(PVC)和对苯二甲酸二邻苯二甲酸酯生产重整产物的新方法,用于民用工程,工业和一般用途的对象的制造

摘要

Invention herewith described refers to the new procedure for the production of regranulates from polyvinyl chloride (PVC) and dioctyl terephthalate for the application in the civil engineering, industry and for the manufacture of objects for general use. The new procedure for production of polyvinyl chloride (PVC) regranulates from polyvinyl chloride (PVC), waste or commercial, and plasticizers synthesized from the waste polyethylene terephthalate (PET), di-(2-ethylhexyl) terephthalate (DOTP) and dichlorinated alkyl terephthalate, shown in Flow sheet 1, begins so that in the reactor - position 1, Flow sheet 1, in the reaction for obtaining di-(2-ethylhexyl) terephthalate (DOTP) or di (alkyl chlorinated) terephthalate, the compound of general formula (I), where R can be 2-ethylhexyl or chlorinated higher fatty alcohols derived from fatty acids of the linseed oil, according to the present invention the waste polyethylene terephthalate (PET), the compound of formula (II),after purification and fragmentation is mixed with alcohol, the compound of general formula (III),where R can be 2-ethylhexyl or chlorinated higher fatty alcohols derived from fatty acids of the linseed oil, whereby with the reaction, with which there are obtained di-(2-ethylhexyl) terephthalate (DOTP) and di(chlorinated alkyl) terephthalates, typically performed in a temperature range from 150° to 250° C, at molar ratio of polyethylene terephthalate (PET) and 1,0:2,0 to 1,0:10,0 of alcohol with or without the use of azeotroping agent for the removal of the reaction water, at the pressure in the reaction vessel from 1.0 to 50.0 bar with or without the presence of a catalyst, and the time necessary to obtain a high conversion degree that can vary from 6 to 24 hours.
机译:本文描述的发明涉及由聚氯乙烯(PVC)和对苯二甲酸二辛酯生产重粒料的新方法,其用于土木工程,工业和用于制造通用物体。新的生产聚氯乙烯(PVC)的程序由废旧或商用的聚氯乙烯(PVC)以及由废对苯二甲酸乙二醇酯(PET),对苯二甲酸二-(2-乙基己基)酯(DOTP)和二氯化对苯二甲酸烷基酯合成的增塑剂进行再生如流程图1所示,开始反应,以便在反应器中-位置1,流程图1中,在用于获得对苯二甲酸二(2-乙基己基)酯(DOTP)或对苯二甲酸二(烷基氯代)酯的反应中,通式为(I),其中R可以是2-亚麻基或亚麻籽油脂肪酸衍生的氯化高级脂肪醇,根据本发明,在纯化和裂解后,废聚对苯二甲酸乙二醇酯(PET),式(II)化合物将其与醇混合,得到通式(III)的化合物,其中R可以是2-乙基己基或衍生自亚麻子油脂肪酸的氯化高级脂肪醇,从而通过反应得到二-(2- Ë对苯二甲酸乙己基酯(DOTP)和对苯二甲酸二(氯化烷基酯),通常在150°至250°C的温度范围内以聚对苯二甲酸乙二醇酯(PET)和1,0:2,0至1,0 ::在有或没有催化剂存在的条件下,在反应容器中的压力为1.0至50.0 bar的条件下,在使用或不使用共沸剂的条件下,将10,0的乙醇用于除去反应水,以及获得高油所需的时间转换程度可能从6到24小时不等。

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