邻—(4—乙基苯甲酰基)苯甲酸的研究

本文阐述了通过Friedel-Crafts反应合成邻-(4-乙基苯甲酰基)苯甲酸的方法.研究了影响产物质量的因素,提出了适宜的工艺条件.     

Biodegradation of monoaromatic hydrocarbons in aquifer columns amended with hydrogen peroxide and nitrate

The ability of indigenous microorganisms to degrade benzene, toluene, ethylbenzene and xylenes (BTEX) in laboratory scale flow-through aquifer columns was tested separately with hydrogen peroxide (110 mg/l) and nitrate (330 mg/l as NO₃⁻) amendments to air-saturated influent nutrient solution. The continuous removal of individual components from all columns relative to the sterile controls provided evidence for biodegradation. In the presence of hydrogen peroxide, the indigeneous microorganisms degraded benzene and toluene (> 95%), meta- plus para-xylene (80%) and ortho-xylene (70%). Nitrate addition resulted in 90% removal of toluene and 25% removal of ortho-xylene. However, benzene, ethylbenzene, meta- and para-xylene concentrations were not significantly reduced after 42 days of operation. Following this experiment, low dissolved oxygen (< 1 mg/l) conditions were initiated with the nitrate-amended column influent in order to mimic contaminated groundwater conditions distal from a nutrient injection well. Toluene continued to be effectively degraded (> 90%), and more than 25% of the benzene, 40% of the ethylbenzene, 50% of the meta- plus para-xylenes and 60% of the ortho-xylene were removed after several months of operation.     

乙苯/苯乙烯塔分离效率问题的技术分析及整改措施

分析了齐鲁分公司200kt/a乙苯/苯乙烯装置乙苯/苯乙烯塔(T-401)分离效率低的原因,即降液管设计偏小,液体在降液管内流速过快,引起液体飞溅;安装分布器使用的石棉垫片溶胀而粉碎后堵塞了分布槽;分布器上使用的垫片脱落形成缝隙而漏液;填料装得不密实,留有缝隙;二级分布槽变形等.针对存在问题提出了相应的整改措施,并考察了整改措施实施效果.结果表明,整改后该塔的分离能力满足了工艺要求,并有一定的操作弹性.     

C8芳烃中二甲苯和乙苯的分离技术进展

论述了用于C8芳烃中二甲苯异构体以及乙苯分离的各种吸附分离技术进展,对各种工艺和特点以及工业应用状况进行了分析比较。详细介绍了目前国内C8芳烃吸附分离装置中的工业生产状况和面临的问题及挑战。提出应抓紧开发具有自主知识产权的C8芳烃吸附分离技术,尤其是开发一种对乙苯和二甲苯同时具有高选择性、高吸附能力、容易脱附的吸附剂,实现从C8芳烃中同时得到乙苯和二甲苯高纯度产品的目的,打破国外的技术垄断。     

微库仑法测定乙苯中的微量硫

以脱硫后的正庚烷为溶剂,采用微库仑法测定乙苯中微量硫的最佳条件为:氩气/氧气为160/40(体积比),进样速度5μL/min,预热温度420℃,燃烧温度760℃,出口区温度640℃,电解液用二次脱盐水配制。微库仑法的准确度和精密度均高于国际标准(ISO)的氢氧焰法。     

Supported Vanadia Catalysts for Dehydrogenation of Ethylbenzene with CO2

Alumina supported vanadia catalysts (V/Al) for selective oxidehydrogenation of ethylbenzene with CO₂ were prepared by impregnation method. During preparation the effect of promoters and calcined temperature was investigated, it was found these two items had a strong influence on the activity of V/Al catalysts. Dehydrogenation reaction with CO₂ was happened in the fixed-bed reactor at 450 °C. Results showed that 15.2% ethylbenzene conversion and 99.2% styrene selectivity were acquired when V₂K/Al catalyst was used.     

Catalytic aerobic oxidation of ethylbenzene over Co/SBA-15

Co(II)O was highly dispersed in the mesopores of SBA-15 by alcoholic impregnation method and characterized by XRD, TEM, UV–VIS DRS, TPR, and XRF techniques. It was found that tetrahedral coordinated Co(II)O was stabilized by SBA-15 at low Co-loading. Co/SBA-15 showed much higher activity than Co(OAc)₂ or Co₃O₄ in the liquid-phase aerobic oxidation of ethylbenzene under solvent-free condition.     

催化裂化干气烃化制二乙苯

在装有100 mL LaZSM5-Al-Mg催化剂的固定床反应器内进行了质量分数为68.5％的苯和质量分数为18.9％的乙苯混合原料与催化裂化干气制二乙苯反应，在反应温度340 ℃、反应压力0.7 MPa、乙苯空速7 h^-1和n(乙苯)∶n(乙烯)=4.5∶1的反应条件下，乙苯不转化，只消耗苯，乙烯转化率在90%左右，对二乙苯选择性和收率分别为85％和75％左右，无邻位二乙苯生成。同时考察了催化剂的运行寿命。     

利用催化裂化干气所含乙烯生产乙苯的技术经济分析

利用催化裂化干气所含乙烯生产乙苯是提高其经济价值的有效途径,从我国催化裂化干气资源看,发展前景乐观;与聚合级乙烯生产乙苯的通用工艺相比较,该技术的生产成本和经济效益具有较强的竞争能力。     

制备方法对Zr-Fe基乙苯脱氢催化剂性能的影响

分别采用浸渍法、溶胶-凝胶法、水热合成法和共沉淀法制备了Al₂O₃负载的Zr-Fe基催化剂25 Zr 5 Fe/Al₂O₃,相应标记为25 Zr 5 Fe/Al₂O₃-imp,25 Zr 5 Fe/Al₂O₃-sol-gel,25 Zr 5 Fe/Al₂O₃-ht和25 Zr 5 Fe/Al₂O₃-cop;对其进行了XRD,BET,H₂-TPR,NH₃-TPD表征,考察了其晶相组成、孔结构、氧化还原性、酸性等性质;将制备的这4种基催化剂用于乙苯脱氢反应中,结合乙苯脱氢活性,简要分析了其构效关系。结果表明：这4种25 Zr 5 Fe/Al₂O₃催化剂的乙苯脱氢催化初始活性顺序与其所含有的中强酸含量高低顺序一致,即从大到小依次为25 Zr 5 ...