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An efficient green route for hexamethylene-1,6-diisocyanate synthesis by thermal decomposition of hexamethylene-1,6-dicarbamate over Co3O4/ZSM-5 catalyst: An indirect utilization of CO2 被引量:4
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作者 Muhammad Ammar Yan Cao +3 位作者 Peng He Liguo Wang Jiaqiang Chen Huiquan Li 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2017年第12期1760-1770,共11页
The utilization of CO2 as raw material for chemical synthesis has the potential for substantial economic and green benefits. Thermal decomposition of hexamethylene-1,6-dicarbamate (HDC) is a promising approach for i... The utilization of CO2 as raw material for chemical synthesis has the potential for substantial economic and green benefits. Thermal decomposition of hexamethylene-1,6-dicarbamate (HDC) is a promising approach for indirect utilization of CO2 to produce hexamethylene-1,6-diisocyanate (HDI). In this work, a green route was developed for the synthesis of HD1 by thermal decomposition of HDC over Co3O4/ZSM-5 catalyst, using chlorobenzene as low boiling point solvent. Different metal oxide supported catalysts were prepared by incipient wetness impregnation (IWI), PEG-additive (PEG) and deposition precipitation with ammonia evaporation (DP) methods. Their catalytic performances for the thermal decomposition of HDC were tested. The catalyst screening results showed that Co3O4/ZSM-525 catalysts prepared by different methods showed different performances in the order of Co3O4/ZSM-5 25(PEG) 〉 Co3O4/ZSM-525(IWI) 〉 Co3O4/ZSM-525(DP). The physicochemical properties of Co3O4/ZSM- 52s catalyst were characterized by XRD, FTIR, N2 adsorption-desorption measurements, NH3-TPD and XPS. The superior catalytic performance of Co3O4/ZSM-52S(PEG) catalyst was attributed to its relative surface content of Co3 +, surface lattice oxygen content and total acidity. Under the optimized reaction conditions: 6.5% HDC concentration in chlorobenzene, 1 wt% Co3O4/ZSM-525(PEG) catalyst, 250℃ temperature, 2.5 h time, 800 ml.min 1 nitrogen flow rate and 1.0 MPa pressure, the HDC conversion and HDI yield could reach 100% and 92.8% respectively. The Co3O4/ZSM-525(PEG) catalyst could be facilely separated from the reaction mixture, and reused without degradation in catalytic performance. Furthermore, a possible reaction mechanism was proposed based on the physicochemical properties of the Co3O4/ZSM-5 25 catalysts. 展开更多
关键词 Hexamethylene-1 6-dicarbamate (HDC)Hexamethylene-1 6-diisocyanate (hdi Thermal decomposition Co3O4/ZSM-5 Heterogeneous catalyst
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Zn-Co bimetallic supported ZSM-5 catalyst for phosgene-free synthesis of hexamethylene–1,6–diisocyanate by thermal decomposition of hexamethylene–1,6–dicarbamate 被引量:1
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作者 Muhammad Ammar Yan Cao +3 位作者 Peng He Li-Guo Wang Jia-Qiang Chen Hui-Quan Li 《Chinese Chemical Letters》 SCIE CAS CSCD 2017年第7期1583-1589,共7页
A set of mono-and bimetallic(Zn-Co) supported ZSM-5 catalysts was first prepared by PEG-additive method. The physicochemical properties of the catalysts were investigated by FTIR, XPS, XRD, N2adsorption-desorption m... A set of mono-and bimetallic(Zn-Co) supported ZSM-5 catalysts was first prepared by PEG-additive method. The physicochemical properties of the catalysts were investigated by FTIR, XPS, XRD, N2adsorption-desorption measurements, SEM, EDS and NH3-TPD techniques. The physicochemical properties showed that the Zn Co2O4 spinel oxide was formed on the ZSM-5 support and provided effectual synergetic effect between Zn and Co species for the bimetallic catalyst. Furthermore, bimetallic supported ZSM-5 catalyst exhibited weak, moderate and strong acidic sites, while the monometallic supported ZSM-5 catalyst showed only weak and moderate or strong acidic sites. Their catalytic performances for thermal decomposition of hexamethylene–1,6–dicarbamate(HDC) to hexamethylene–1,6–diisocyanate(HDI) were then studied. It was found that the bimetallic supported ZSM-5 catalysts,especially Zn-2Co/ZSM-5 catalyst showed excellent catalytic performance due to the good synergetic effect between Co and Zn species, which provided a suitable contribution of acidic sites. HDC conversion of 100% with HDI selectivity of 91.2% and by-products selectivity of 1.3% could be achieved within short reaction time of 2.5 h over Zn-2Co/ZSM-5 catalyst. 展开更多
关键词 Hexamethylene–1 6–dicarbamate(HDC) Hexamethylene–1 6diisocyanate(hdi) Thermal decomposition Bimetallic supported ZSM-5 catalyst Synergetic effect
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非光气法制备HDI工艺研究进展 被引量:6
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作者 刘喆 王庆印 王公应 《天然气化工—C1化学与化工》 CAS CSCD 北大核心 2016年第4期94-98,共5页
对非光气法制备六亚甲基-1,6-二异氰酸酯(HDI)的各种技术路线进行综述。重点对氨基甲酸酯热解制备HDI的工艺、催化剂、溶剂及添加剂等进行详细评述,并对HDI清洁生产技术的发展趋势进行展望。
关键词 氨基甲酸酯 六亚甲基-1 6-二异氰酸酯(hdi) 催化剂 热分解 综述
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HDI合成工艺进展 被引量:9
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作者 王慧宁 王建龙 曹端林 《山西化工》 2006年第1期14-18,共5页
综述了六亚甲基二异氰酸酯(HDI)的几种主要合成工艺,并对其优缺点进行了分析,着重介绍了光气法和六亚甲基二氨基甲酸甲酯(HDU)热解法。
关键词 六亚甲基二异氰酸酯(hdi) 光气 六亚甲基二氨基甲酸甲酯(HDU) 热解
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HDI-TMP加成物的合成 被引量:1
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作者 阎宏永 宋文生 +1 位作者 李雪娟 李国芝 《广州化工》 CAS 2007年第5期25-28,共4页
研究了耐候性聚氨酯涂料固化剂六亚甲基二异氰酸酯-三羟甲基丙烷(HDI-TMP)加成物的合成工艺。通过对反应产物NCO含量和粘度的测定,考察了TMP中水分含量、反应温度、反应时间、HDI与TMP摩尔比、催化剂对加成产物的影响。实验表明,TMP中... 研究了耐候性聚氨酯涂料固化剂六亚甲基二异氰酸酯-三羟甲基丙烷(HDI-TMP)加成物的合成工艺。通过对反应产物NCO含量和粘度的测定,考察了TMP中水分含量、反应温度、反应时间、HDI与TMP摩尔比、催化剂对加成产物的影响。实验表明,TMP中水分对加成产物粘度影响很大,因此TMP需进行脱水处理;HDI-TMP加成物合成最佳工艺条件为:催化剂二月桂酸二丁基锡(DBTDL)用量0.05%,HDI与TMP的摩尔比≥3.15,反应温度80℃,反应时间3h,可获得低粘度HDI-TMP加成物。 展开更多
关键词 六亚甲基二异氰酸酯(hdi) 三羟甲基丙烷(TMP) hdi-TMP加成物 粘度 NCO含量
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己二异氰酸酯-三羟甲基丙烷加成物的合成
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作者 宋文生 阎宏永 +1 位作者 李雪娟 李国芝 《信阳师范学院学报(自然科学版)》 CAS 北大核心 2008年第1期129-132,共4页
研究了耐候性聚氨酯涂料固化剂己二异氰酸酯(HDI)-三羟甲基丙烷(TMP)加成物的合成工艺.通过对反应产物NCO含量和黏度的测定,考察了TMP中水分含量、催化剂、HDI与TMP摩尔比、反应温度、反应时间对加成产物的影响.结果表明,TMP中水分对加... 研究了耐候性聚氨酯涂料固化剂己二异氰酸酯(HDI)-三羟甲基丙烷(TMP)加成物的合成工艺.通过对反应产物NCO含量和黏度的测定,考察了TMP中水分含量、催化剂、HDI与TMP摩尔比、反应温度、反应时间对加成产物的影响.结果表明,TMP中水分对加成产物黏度影响很大,需进行脱水处理;HDI-TMP加成物最佳合成工艺条件为:催化剂二月桂酸二丁基锡用量0.05%,HDI与TMP的摩尔比3.15,反应温度80℃,反应时间3 h,可获得低黏度HDI-TMP加成物. 展开更多
关键词 己二异氰酸酯(hdi) 三羟甲基丙烷(TMP) hdi—TMP加成物 黏度 NCO含量
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