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提出一种以负载型Ni-Cr-B非晶态合金催化对氯硝基苯加氢制备对氯苯胺的工艺。通过正交实验考察反应温度、反应时间、反应压力和催化剂用量对对氯苯胺收率的影响。最优工艺条件为:反应温度60℃,反应时间4 h,反应压力1.2 MPa,催化剂用量占对氯硝基苯质量的8%。在此优化条件下,催化剂重复使用4次,对氯硝基苯转化率为99.9%,对氯苯胺选择性为99.9%,对氯苯胺平均收率为99.8%。 相似文献
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SRNA-4非晶态合金催化双环戊二烯液相加氢反应研究 总被引:3,自引:0,他引:3
采用SRNA-4非晶态合金催化剂对双环戊二烯(DCPD)进行了加氢反应考察,研究了搅拌速度、温度、压力和催化剂浓度各条件对双环戊二烯加氢反应的影响.结果表明DCPD加氢反应为连串反应,中间产物主要为9,10-二氢双环戊二烯(9,10-DHDCPD)和少量1,2-二氢双环戊二烯(1,2-DHDCPD);DCPD易于加氢生成中间产物9,10-DHDCPD,其继续加氢为四氢双环戊二烯(endo-THDCPD)需要较为剧烈的条件.DCPD加氢过程选用两段法,第一段为温度110℃,第二段为130℃,压力均为1.5MPa,催化剂浓度1.18%.非晶态合金(催化剂)对DCPD的加氢反应活性明显高于Raney Ni,可进行1、2位加氢反应生成1,2-DHDCPD,并且催化剂用量少,反应温度和反应压力低,反应时间短,生成副产物少. 相似文献
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《化学工业与工程技术》2020,(3):9-14
采用负载型Ru/Al_2O_3催化剂对双酚A(BPA)加氢制备氢化双酚A(HBPA)进行了研究,考察了催化剂煅烧温度、煅烧时间、还原温度、还原时间、催化剂负载量等制备条件对反应的影响,确定催化剂最佳制备条件为:煅烧温度200℃、煅烧时间5 h、还原温度100℃、还原时间1 h,Ru负载量(w)3%。同时考察了溶剂类型、催化剂用量、反应温度、反应压力等条件对催化加氢反应的影响,确定催化加氢反应的最佳工艺条件为:溶剂选用异丙醇、催化剂用量3%、反应温度160℃、反应压力4.5MPa、反应时间4 h。在上述最佳条件下,双酚A的转化率为100%,氢化双酚A的选择性为97.08%。 相似文献
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本文介绍了精棉油催化加氢的试验结果。研究了反应温度、反应压力及催化剂用量对氢化反应的影响。试验表明KE—NF—20催化剂用于棉籽油加氢,是一种活性和选择性好的催化剂。在反应温度为220~240℃,反应压力O.8~1.0Mpa,催化剂用量0.2~0.3%条件下,短时间内可完成极度氢化的反应,氢化油碘值降于2mg/g以下。 相似文献
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详细研究了空气气氛下、30~60℃、 THF溶液中贮氢合金催化丁腈橡胶双键加氢的宏观动力学.通过一系列不同反应温度下的实验结果获得了贮氢合金催化丁腈橡胶加氢反应的表观活化能(48.74 kJ8226;mol-1),较低的表观活化能表明在贮氢合金催化丁腈橡胶溶液加氢反应中,反应物较易活化且反应具有较低的温度敏感性.利用IR和1HNMR研究了贮氢合金催化丁腈橡胶双键加氢的选择性,结果表明1,4-BD单元较1,2-BD单元优先加氢,同时给出了trans-1,4-BD和1,2-BD加氢的动力学研究结果.根据动力学及其他研究结果提出了可能的反应机理,该机理较好地解释了反应中出现的现象. 相似文献
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Chandra Mouli R. Madhuranthakam Qinmin Pan Garry L. Rempel 《American Institute of Chemical Engineers》2009,55(11):2934-2944
A continuous process for hydrogenating nitrile butadiene rubber (NBR) was developed and its performance was experimentally investigated. A Kenics® KMX static mixer (SM) is used in the process as a gas–liquid reactor in which gaseous hydrogen reacts with NBR in an organic solution catalyzed by an organometallic complex such as an osmium complex catalyst. The Kenics® KMX SM was designed with 24 mixing elements with 3.81 cm diameter and arranged such that the angle between two neighboring elements is 90°. The internal structure of each element is open blade with the blades being convexly curved. The dimensions of the SM reactor are: 3.81 cm ID 80 S and 123 cm length and was operated cocurrently with vertical upflow. The NBR solutions of different concentrations (0.418 and 0.837 mol/L with respect to [C?C]) were hydrogenated by using different concentrations of the osmium catalyst solution at various residence times. The reactions were conducted at a constant temperature of 138°C and at a constant pressure of 3.5 MPa. From the experimental results, it is observed that a conversion and/or degree of hydrogenation above 95% was achieved in a single pass from the designed continuous process. This is the first continuous process for HNBR production that gives conversions above 95% till date. Optimum catalyst concentration for a given mean residence time to achieve conversions above 95% were obtained. Finally, a mechanistic model for the SM reactor performance with respect to hydrogenation of NBR was proposed and validated with the obtained experimental results. © 2009 American Institute of Chemical Engineers AIChE J, 2009 相似文献
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The catalytic hydrogenation of acrylonitrile‐butadiene copolymer (nitrile rubber, NBR) using Pd(OAc)2 or RuCl2(PPh3)3 catalysts has been investigated in order to produce a totally saturated nitrile rubber. The hydrogenation of NBR is effective with both catalysts and achieved total conversion under the appropriate reaction conditions. In the case of palladium the effects of reaction parameters such as reaction temperature, pressure, time, catalyst concentration, and NBR concentration have been investigated. Even though both ruthenium‐ and palladium‐based catalysts are effective in the production of HNBR, the former requires harsh reaction conditions and has the drawback of gel formation under high conversion, motivating the migration to RuCl2 (PPh3)3 as an alternative catalyst. The degree of hydrogenation was determined by IR and NMR spectroscopy. © 2007 Wiley Periodicals, Inc. J Appl Polym Sci, 2007 相似文献
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Xunzhang Wang Liqun Zhang Yang Han Xiangke Shi Weimin Wang Dongmei Yue 《应用聚合物科学杂志》2013,127(6):4764-4768
A new hydrogenation system consisting of hydrazine hydrate and sodium periodate has been developed for hydrogenation of nitrile‐butadiene rubber (NBR) latex by diimide reduction technique. The optimization of the reaction conditions was obtained. The influences of the concentration of reactants, reaction time, and temperature on hydrogenation degree were investigated. The results indicated that hydrogenation degree of the product (HNBR) can be extended to 95% through this new method. In addition, 1H‐NMR and infrared spectra confirmed that C?C double bonds in NBR were successfully hydrogenated without reduction of the CN group. © 2012 Wiley Periodicals, Inc. J. Appl. Polym. Sci., 2013 相似文献
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研究了各种反应条件对贮氢合金MINi5-x(CoMnAl)x的氢化物对丁腈橡胶溶液双键加氢的影响。随着反应温度升高氢化度也提高;当舍金氢化物超过理论用量的2倍时,氢化度与催化剂的用量无关;氢化度与反应时间不是简单的线性关系;关于溶剂的影响,发现溶剂为氯仿时无加氢反应发生,而在四氢呋喃中则可得到具有较高氢化度的产物。此外还发现丁腈橡胶氢化度受反应气氛、氢压等因素的影响。 相似文献
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研究了共轭二烯烃类聚合物在贮氢合金氢化物存在下双键加氢的情况。结果表明AB;型贮氢合金[包括LaNi5和MINi5-x(CoMnAl)8]可催化NBR、NR、BR、SBS等共轭二烯烃聚合物双键加氢,其氢化度分别可达33.5%、31.1%、45.8%、32.3%。采用IR、^1H NMR、碘量分析法等手段对加氢产物进行了分析,表明聚合物中双键加氢的同时,NBR中的-C≡N和SBS中的苯环不受影响。此外。研究结果还表明合金组成、表面处理方式等对贮氢合金催化共轭二烯烃类聚合物双键加氢活性有影响。合金氢化物在共轭二烯烃类聚合物双键加氢过程中具有提供氢源与催化双重功能。 相似文献
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以20%的拟薄水铝石为黏结剂制备新型固定床Raney镍催化剂,采用苯加氢为模型反应,研究了前驱物成型合金浸取条件对催化剂加氢活性的影响.实验结果表明,对于860℃焙烧2 h后的成型合金,以10%~20%的NaOH溶液在80~90℃浸取3~4 h可得到具有较高加氢活性的固定床Raney镍催化剂.浸取反应可在1~4 h内基本完成,浸取后催化剂表面出现微孔结构,具有较好的苯加氢活性和活性稳定性,可在120℃、0.5 MPa、空速2 h-1的缓和条件下实现苯的完全转化. 相似文献
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影响偶氨法常压氢化丁苯胶乳氢化度及凝胶的因素 总被引:1,自引:0,他引:1
研究了采用水合肼(N2H2·H2O)/H2O2/CuSO4使冷法聚合丁苯胶乳在常压下氢化的各种条件,包括乳化剂种类及用量、催化剂CuSO4的用量、N2H4·H2O及H2O2的用量、反应温度及反应时间等对氢化丁苯橡胶氢化度及凝胶含量的影响。结果表明,当加入质量分数为0 8%的十二烷基苯磺酸钠乳化剂,CuSO4催化剂用量为0.0025 mmol/g,反应温度为55℃,反应时间为7h,N2H4/C=C之摩尔比为1.8,H2O2/N2H4之摩尔比为1.5时,可得到氢化度为98%。凝胶质量分数小于0.6%的氢化丁苯橡胶。 相似文献
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S. Koritala K. J. Moulton Sr. J. P. Friedrich E. N. Frankel W. F. Kwolek 《Journal of the American Oil Chemists' Society》1984,61(5):909-913
Selective hydrogenation of soybean oil to reduce linolenic acid is accomplished better with copper than with nickel catalysts.
However, the low activity of copper catalysts at low pressure and the high cost of batch equipment for high-pressure hydrogenation
has precluded their commercial use so far. To evaluate continuous systems as an alternative, soybean oil was hydrogenated
in a 120 ft × 1/8 in. tubular reactor with copper catalyst. A series of hydrogenations were performed according to a statistical
design by varying processing conditions: oil flow (0.5 L/hr, 1.0 L/hr and 2.0 L/hr), reaction temperature (180 C and 200 C),
hydrogen pressure (1,100 psig and 4,500 psig) and catalyst concentration (0.5% and 1.0%). An iodine value (IV) drop of 8–43
units was observed in the products whereas selectivity varied between 7 and 9. Isomerization was comparable to that observed
with a batch reactor. Analysis of variance for isomerization indicated interaction between catalyst concentration and hydrogen
pressure and between catalyst concentration and temperature. The influence of pressure on linolenate selectivity was different
for different temperatures and pressure. Hydrogenation rate was significantly affected by pressure, temperature and catalyst
concentration. 相似文献
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本文研究了4,4'-二硝基二苯乙烯-2,2'-二磺酸(DNS酸),在Pt/C催化剂存在下,Zn和Cu为抑制剂,水相体系中液相催化加氢制备DSD酸。Pt-Cu-Zn/C催化剂制备DSD酸具有很好的活性和选择性,能有效抑制苄基物及影响色度的杂质的生成。较佳的工艺条件为:DNS酸钠盐质量浓度为12~20%、Pt/C催化剂量为硝基物的0.5~0.7%,反应温度40~60℃、pH4~6、氢气压力1.0 MPa。DNS酸转化率100%,DSD酸选择性98.5%以上,收率98%,DSD酸含量均达到95%以上(氨基值法),苄基物含量低于0.1%(外标法),色度低于0.2。新工艺生产每吨DSD酸产生废水12吨,废水COD值为24 mg/L,无色透明。 相似文献