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本文着重介绍了氟乙烷的各种制备方法,对各种工艺进行了比较,以期从中选出适合于工业生产的工艺方法;文中也对氟乙烷的各种性质和用途进行了简单的介绍. 相似文献
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The treatment or upgrading of waste trifluoromethane (CHF3, R23), which has a significant greenhouse effect, is of great importance in industry. Herein, series of SO42−/ZrO2-SiO2 catalysts with different Brønsted and Lewis acid site densities and ratios were prepared for pyrolysis of R23 to tetrafluoroethylene (C2F4, TFE) and hexafluoropropylene (C3F6, HFP). The effects of impregnation concentration of (NH4)2SO4 on specific surface area, crystal phase, and Brønsted and Lewis acid site densities and ratios were respectively demonstrated. The Brønsted and Lewis acid sites were observed to have cooperative effects on R23 transformation and up to 94.6% selectivity of (TFE + HFP) could be achieved at 750°C. The kinetic studies revealed the decomposition of R23 into CF2 carbene and HF was the rate-determining step, and a deactivation behavior was found due to the site coverage and pore blockage by the oligomers of TFE and HFP. 相似文献
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A flow cell was used for the in situ ESR monitoring of the state and reactivity of chromium ions in Cr-ZSM-5. Calcination of Cr(NO3)3/NH4-ZSM-5 in air at 500°C is accompanied by migration of chromium ions inside the zeolitic channels and stabilization ofisolated Cr5+ cations near lattice A13+ ions. Calcination of Cr-ZSM-5 at 750°C leads to a gradual disappearance of the isolated Cr5+ cations and formation of -Cr2O3 microcrystals. All the Cr5+ cations are accessible to gas-phase molecules: O2 strongly broadens the dipole-dipole signal; H2O sorption increases the local crystal field symmetry; admission of CCl4 results in a small change of the Cr5+ local coordination; strongly stabilized complexes on Cr-ZSM-5 are observed upon sorption of either NO or NO2. The sorption of C2H6 on Cr-ZSM-5 at 20°C is accompanied by a gradual reduction of the Cr5+ sites. At 500°C in [C3H6 + O2 + He] flow, even at a large excess of oxidant, the reduction of a noticeable part of Cr5+ ions takes place. At 400°C, in the same gas mixtures, a deeper reduction of Cr5+ occurs. Closer to stoichiometric conditions, in a [C3H6 + NO + He] flow with 120% excess of oxidant the Cr5+ is completely reduced at 500°C. The oxidation of propene is accompanied by coke deposition on the surface of the catalyst. The implications of the results are discussed. 相似文献
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本文主要介绍了国内外对乙烯联产混合C4、C5烃的利用。并由此转化为高值化产品,降低乙烯生产成本,提高经济效益 相似文献
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简要介绍了2-丙基庚醇(2-PH)生产技术及生产工艺,2-PH的市场需求和应用前景。2-PH装置作为对煤化工副产混合碳四的综合利用装置,分析其技术经济性,并对项目建设提出建议。 相似文献
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试析C4钢N_2O_4冷凝器腐蚀原因宋尔应(淮南化工总厂安徽省淮南市232038)我厂于1990年8月将浓硝酸生产设备N2O4冷凝器的材质由高纯铝更新为C4钢(00Cr14Ni14Si4),结构如图1所示。该设备运行到1992年7月1日,在浓硝酸停车... 相似文献
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测量了25 C时CaC_2O_4-H_2C_2O_4-H_2O三元系的固液平衡数据,实验数据用Pitzer模型进行了关联。 相似文献
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本文报导含类立方烷型簇核Fe4S4的金硫配位化合物「(C2H5)4N2「Fe4S4」S2CN(C2H5)2」4」的合成,晶体和分子结构测定的结果。 相似文献
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将焦宝石粉、活性炭粉和铝粉按质量比39:27.6:33.4配料作为基料,再分别加入占基料总质量0、3%、6%和9%的TiO2粉末(锐钛矿型),加入<10%的酚醛树脂为结合剂混匀后,压制成型,坯体试样干燥后,置于刚玉管式炉中,通入流动氩气,分别于1 300、1 400、1 500、1 600和1 700℃保温2 h制备了Al4SiC4-Al4O4C复合材料.利用热重分析、化学分析、XRD和SEM等测试技术,研究了TiO2加入量对材料物相组成和显微结构的影响.结果表明:试样中的Ti在烧成过程中有少量损失,残余的TiO2在1 300 ℃前全部反应转变为TiC,生成的TiC在1 300~1 700 ℃稳定存在;Tio2加入量对材料物相组成没有明显影响,但TiO2加入量超过3%时,Al4SiC4和Al4O4C的生成温度将由1 500℃提升至1 600℃;随着材料中Ti4+浓度增加,Ti4+更容易与Al4SiC4形成有限置换固溶体而导致晶格缺陷,促使Al4SiC4在1 700℃分解,形成更多的Al4O4C短纤维,同时使试样表面生成片状Al2O3层. 相似文献
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以B4C与Si3N4和少量SiC,TiC为原料,Al2O3和Y2O3为烧结助剂,烧结温度为1 800~1 880℃,压力为30 MPa的热压条件下制备(SiC,TiB2)/B4C复合材料.用透射电子显微镜、扫描电子显微镜和能谱分析进行显微结构分析.结果表明:在烧结过程中反应生成了SiC,TiB2和少量的BN.复合材料的主晶相之间有长棒状架构弥散相和束状弥散相,在部分B4C晶粒内部出现了内晶结构.结合对复合材料性能的分析表明:新形成相、均匀细晶和棒状结构对提高材料的性能具有重要作用.通过对材料断口形貌和裂纹扩展模式分析认为,复合材料的断裂机制主要为裂纹偏转. 相似文献
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(NH4)2C2O4·H2O和NH4HC2O4·0.5H2O 单晶的培养研究 总被引:1,自引:0,他引:1
利用六次甲基四胺缓慢水解产生的NH3和草酸反应,扩散法培养出(NH4)2C2O4·H2O和NH4HC2O4·0.5H2O两种单晶. 相似文献
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Yun-Jo Lee Jo-Yong Park Ki-Won Jun Jong Wook Bae Nagabhatla Viswanadham 《Catalysis Letters》2008,126(1-2):149-154
An attempt made for the selective production of C2–C4 olefins directly from the synthesis gas (CO + H2) has led to the development of a dual catalyst system having a Fischer–Tropsch (K/Fe–Cu/AlOx) catalyst and cracking (H-ZSM-5) catalyst operate in consecutive dual reactors. The flow rate (space velocity) and H2/CO molar ratio of the feed have been optimized for achieving higher CO conversions and olefin selectivities. The selectivity to C2–C4 olefins is further enhanced by optimizing the reaction temperature in the second reactor (cracking), where the product exhibited 51% selectivity to C2–C4 hydrocarbons rich in olefins (77%) with a stable time-on-stream performance in a studied period of 100 h. 相似文献