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《化学工业与工程技术》2020,(3)
<正>申请号:CN201811444140.2申请日:20181129申请人:中国石油化工股份有限公司;中国石油化工股份有限公司北京化工研究院本发明属于催化剂领域,更具体地,涉及一种含镁/钛的固体催化剂组分及其制备方法和烯烃聚合催化剂及其应用。所述含镁/钛的固体催化剂组分的制备方法包括将卤化镁、有机环氧化合物、有机磷化合物和惰性稀释剂Ⅰ混合并进行第一反应,往所得第一反应产物中依次加入助析出剂、惰性稀释剂Ⅱ和钛的卤化物进行第二反应,之后 相似文献
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综述了带有芳氧基亚胺配体的ⅣB族金属络合物(FI催化剂)催化的乙烯类共聚合。Ti-FI催化剂可用于乙烯与α-烯烃、乙烯与环烯烃的共聚合。相比传统的茂金属催化剂,FI催化剂可以制备共聚单体含量更高的共聚物。FI催化剂对极性基团具有良好的耐受性,将其用于乙烯与极性单体的共聚合,可取得理想的效果。与亚胺N原子相连的芳香环上的邻位H原子被F原子所取代的Ti-FI催化剂催化乙烯类聚合时,表现出活性聚合的特征。因此可通过控制单体加入顺序制备嵌段共聚物。用两种不同的FI催化剂,且以二乙基锌为链穿梭剂,可制备多嵌段共聚物。优化配体结构可制备高效的乙烯类共聚合催化剂。这些将有利于实现聚烯烃的功能化和高性能化。 相似文献
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在国产阳原活性炭上浸渍乙酸锌溶液,以制备新的用于乙炔法生产乙酸乙烯的催化剂,得到了一个包含浸渍时间、浸渍比、浸渍温度、浸渍初始浓度的经验公式。选择了内循环无锑度反应器,对该国产乙炔法合成乙酸乙烯新型催化剂进行了评价,并选定了动力学实验条件,探索该国产催化剂和进口的BPL型催化剂上反应温度和分压对反应速率影响的规律,从而建立宏观动力学方程。 相似文献
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研究了不同碱催化剂催化合成聚氧乙烯(PEG)与聚氧乙烯-丙烯共聚醚(PEPG)的反应,考察了镁铝复合氧化物的制备条件对催化性能的影响,通过凝胶色谱仪(GPC)对产品分子量及分布情况进行了分析。结果表明,催化制备聚氧乙烯研究中,以KOH、镁铝复合氧化物的催化效果较好;催化制备氧化乙烯-氧化丙烯共聚醚研究中,以NaOH、镁铝复合氧化物的催化效果较好;制备镁铝复合氧化物催化剂时,当以Na2CO3,NaOH为共沉淀剂,镁铝物质的量比3∶1,煅烧温度550℃时,制备的镁铝复合氧化物催化剂催化性能最佳。 相似文献
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制备了一种新型高氢调敏感性乙烯淤浆聚合用催化剂(简称SEL催化剂)。考察了SEL催化剂的组成、粒子形态,催化乙烯均聚合与共聚合的性能,以及用其制备的聚乙烯的性能,并与商业化的同类型进口催化剂(简称参比催化剂)进行了对比。结果表明:SEL催化剂中钛含量高而镁含量低,粒径分布窄,颗粒形态规整;SEL催化剂催化乙烯聚合时氢调敏感性好,氢气分压为0.48 MPa,乙烯分压为0.25 MPa时,聚乙烯熔体流动速率达226.10g/10 min;SEL催化剂催化乙烯与1-己烯共聚合的性能和聚乙烯粉料中细粉含量等均优于参比催化剂。 相似文献
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采用NaOH溶液对含粘结剂的成型工业MCM-22分子筛催化剂进行后处理以脱除粘结剂,制备无粘结剂MCM-22分子筛催化剂,并实验考察了碱浓度、处理时间对催化剂的强度、活性组分的含量、酸量及催化性能的影响。结果表明:在NaOH溶液的质量分数为0.3%、150℃的条件下对圆柱形含粘结剂MCM-22分子筛催化剂处理4h,即可制得无粘结MCM-22分子筛催化剂。在苯与乙烯液相烷基化反应中,在苯与乙烯物质的量比为3.0,乙烯质量空速为9.0h~(-1),温度200℃,压力3.5 MPa的反应条件下,无粘结剂MCM-22分子筛催化剂的乙烯转化率维持在60%以上,催化性能与分子筛原粉相当,明显优于含粘结剂的催化剂(低于40%),且其强度能够满足工业应用的要求。 相似文献
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在MgCl2溶解过程中加入内给电子体,开发了一种新型丙烯聚合用BCZ型催化剂,并在5 L聚合釜中进行了本体聚合考核评价,在12 m3小本体工艺装置上进行工业应用试验,在25 kg/h的连续法Innovene气相工艺装置进行中试试验。研究表明:用BCZ型催化剂制备聚丙烯(PP)时,催化剂活性高出国产同类催化剂近50%,氢调敏感性好,同样氢气用量下,PP的熔体流动速率可提高25%左右;所制PP的相对分子质量分布大于7.5,等规指数高;BCZ型催化剂可用于小本体法工艺、连续法气相工艺装置制备均聚和共聚PP。 相似文献
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Preparation of heavy oil hydrotreating catalyst from spent residue hydroprocessing catalysts 总被引:1,自引:0,他引:1
In recent years, increasing emphasis has been placed on recycling spent hydroprocessing catalysts due to environmental regulations which list them as hazardous waste materials. In the present work, the recycling of spent residue hydroprocessing catalysts that contained high levels of vanadium was investigated by using them in the preparation of active new hydrotreating catalyst after subjecting them to different treatments such as decoking, acid-leaching and hydrothermal treatment. Catalyst extrudates containing different levels of V, Mo and Ni on Al2O3 were prepared by mixing the spent catalyst powder with boehmite in different proportions followed by peptization, kneading and extrusion. The prepared catalyst extrudates were characterized by chemical analysis and surface area and porosity measurements. The HDS and HDM activities of the catalysts were tested using Kuwait atmospheric residue as feed and compared with that of a reference HDM catalyst. Partial leaching of vanadium from the spent catalyst opened up the pores, and the catalyst prepared by mixing the metal-leached spent catalyst (MLSC) with boehmite had higher surface area and pore volume and showed higher hydrotreating activity than that prepared from unleached spent catalyst. Hydrothermal treatment of the spent catalyst increased its porosity and surface area. Catalysts prepared from hydrothermally treated spent catalyst (HTSC) had higher surface area and pore volume and showed higher HDM and HDS activities than that prepared from the spent catalyst without hydrothermal treatment. The catalysts prepared from the treated spent catalysts also exhibited substantially higher HDM and HDS activities than the reference commercial HDM catalyst. The results indicate that spent catalysts containing high levels of vanadium together with Mo and Ni on Al2O3 can be used in the preparation of active HDM/HDS catalysts, and thereby, their environmental problem can be reduced. 相似文献
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FDAs-1脱砷剂的研究与开发 总被引:3,自引:0,他引:3
研制出与中国石化抚顺石油化工研究院加氢精制催化剂相配套的FDAs-1预精制脱砷催化剂。对硫化态或氧化态两种形态脱砷剂的实验表明,FDAs-1具有很高的脱砷活性。在工业应用时,可直接在重整氢条件下用氧化态脱砷剂开车。反应温度和氢油比对FDAs-1脱砷剂的性能有明显的影响。反应温度上升,氢油比增大,脱砷率显著提高。反应压力以及空速对催化剂脱砷活性的影响不大。在1.5~2.0 MPa、290 ℃、空速6~12 h-1条件下,硫化态脱砷剂在1000 h内脱砷率高于99%。 相似文献