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以3,5-二硝基苯甲酰氯、3-氨基丙酸和6-氨基正己酸为原料,室温反应合成了3-(3,5-二硝基苯甲酰氨基)丙酸和6-(3,5-二硝基苯甲酰氨基)正己酸。反应过程中,3,5-二硝基苯甲酰氯分批加入,滴加2 mol/L氢氧化钠水溶液控制反应体系的pH=8~9,n(3,5-二硝基苯甲酰氯)/n(氨基酸)=1,收率分别为84%和81%;硝基化合物经10%钯炭催化剂(用量为反应物质量的10%)催化加氢,再经盐酸酸化,得目标产物3-(3,5-二氨基苯甲酰氨基)丙酸盐酸盐和6-(3,5-二氨基苯甲酰氨基)正己酸盐酸盐,收率分别为93%和94%。相关化合物的结构通过FTIR1、HNMR1、3CNMR进行了表征。 相似文献
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以醛、酮为原料经羟醛缩合反应合成了具有一类含查尔酮结构的光敏性二胺:1-(3-氨基苯基)-3-(4-氨基苯基)-2-丙烯-1-酮与对-二(间氨基肉桂酰)苯.通过优化实验得到最佳的合成工艺为:醛、酮在温度为0℃下,以乙醇为溶剂,氢氧化钠为催化剂,进行羟醛缩合反应3h.收率可达到86%,经液相色谱分析其纯度分别为99.92%,99.91%,紫外可见最大吸收波长分别为349nm、361nm.所得方法操作简便,收率较高,原料易得.并用元素分析、核磁共振、红外光谱等手段对产物的结构进行了表征. 相似文献
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(S) 2 氨基 4 (甲硫基)丁酸甲酯盐酸盐于浓氨水中,发生酰胺化反应,制得(S) 2 氨基 4 (甲硫基)丁酰胺,收率63%;(S) 2 氨基 4 (甲硫基)丁酰胺用甲醇溶解,与浓盐酸成盐,得(S) 2 氨基 4 (甲硫基)丁酰胺盐酸盐,收率66%;(S) 2 氨基 4 (甲硫基)丁酰胺盐酸盐在相转移催化剂四丁基溴化铵(TBAB)及研细氢氧化钾的作用下,与4 氯丁酰氯发生取代、环化反应,制得(S) 4 (甲硫基) 2 [2 羰基 1 吡咯烷基]丁酰胺,收率61%。产品的结构经TLC、IR、1HNMR等进行了表征。 相似文献
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2-氨基乙基-二(3-氨基丙基)胺的合成工艺研究 总被引:9,自引:0,他引:9
利用氨基乙腈及丙烯腈的亲核加成、氢化反应合成了一种新的不等臂有机多胺化合物 2 -氨基乙基 -二 (3-氨基丙基 )胺。研究了不同工艺条件对反应的影响 ,最佳工艺条件为 :n(丙烯腈 )∶n(氨基乙腈 ) =2 .8~ 3 .0 ,加成温度为 70~ 75℃ ,加成反应时间为 50~ 60h ,催化反应采用复合催化剂 ,m(溶剂 )∶m(物料 )≈ 1 0。两步反应的收率分别为 81 .6 %和 71 .6 % ,用多种谱学手段表征确证了该化合物及其中间产物 相似文献
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以L-天冬氨酸和乙酸酐为原料,经脱水环化合成N-乙酰-L-天冬酸酐,然后与对氨基苯甲酸经N-酰化反应合成得到新化合物4-(2-乙酰氨基-3-羧基丙酰氨基)苯甲酸。通过Scifinder查询,未发现它的报道。研究了物料配比、反应温度、反应时间和溶剂等因素对产物收率的影响。优化条件为:无水乙醇作溶剂,n(N-乙酰-L-天冬酸酐)∶n(对氨基苯甲酸)=1∶1,反应温度为45℃,反应时间为3 h。优化条件下产物收率为78.7%。目标化合物经熔点、红外和核磁氢谱确证。 相似文献
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我厂3号回转窑(Φ4m×60m)生产线在1996年年底由SP窑(产量912t/d)改为NSP窑(产量1320t/d),预分解系统为四级旋风预热器带离线式分解炉 相似文献
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乙烯酮(双乙烯酮)是十分重要的化工中间体,其下游产品较多。江苏某化工厂开发生产乙烯酮(双乙烯酮)下游产品三十多个,年生产规模三万多吨,是国内以乙烯酮(双乙烯酮)为中间体生产精细化学品的综合骨干企业。针对乙烯酮(双乙烯酮)下游产品废水特点,该厂结合企业实际,开展了产品优化,结构调整,清洁生产,资源循环利用,节水降耗等工作,从源头削减了污染物的生产。同时投资二千多万元新建预处理装置三套,6000m3/d废水生化处理装置一套,使全厂乙烯酮(双乙烯酮)下游产品的废水得到了有效的治理。 相似文献
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The objective of the study was to explore the effect of the degree of deacetylation (DD) of the chitosan used on the degradation rate and rate constant during ultrasonic degradation. Chitin was extracted from red shrimp process waste. Four different DD chitosans were prepared from chitin by alkali deacetylation. Those chitosans were degraded by ultrasonic radiation to different molecular weights. Changes of the molecular weight were determined by light scattering, and data of molecular weight changes were used to calculate the degradation rate and rate constant. The results were as follows: The molecular weight of chitosans decreased with an increasing ultrasonication time. The curves of the molecular weight versus the ultrasonication time were broken at 1‐h treatment. The degradation rate and rate constant of sonolysis decreased with an increasing ultrasonication time. This may be because the chances of being attacked by the cavitation energy increased with an increasing molecular weight species and may be because smaller molecular weight species have shorter relaxation times and, thus, can alleviate the sonication stress easier. However, the degradation rate and rate constant of sonolysis increased with an increasing DD of the chitosan used. This may be because the flexibilitier molecules of higher DD chitosans are more susceptible to the shear force of elongation flow generated by the cavitation field or due to the bond energy difference of acetamido and β‐1,4‐glucoside linkage or hydrogen bonds. Breakage of the β‐1,4‐glucoside linkage will result in lower molecular weight and an increasing reaction rate and rate constant. © 2003 Wiley Periodicals, Inc. J Appl Polym Sci 90: 3526–3531, 2003 相似文献
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Conclusions It is significant that the purification on a single passage of viscose through porous ceramic corresponds to the result of a two-stage filtration of it in industrial filter-presses with standard fillings.Kiev Combine. Kiev Technological Institute of Light Industry. Translated from Khimicheskie Volokna, No. 3, pp. 20–22, May–June, 1969. 相似文献
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A refined nonlinear value of the main parameter of a material, i.e., the elongation modulus versus the instant temperature value, was suggested for introduction into the computational algorithm of tempering stresses. 相似文献