氧化钴／吸附树脂催化剂在对甲酚氧化反应中的催化性能研究

本文研究了吸附树脂D3520负载的氧化钴催化剂对甲酚氧化反应中的催化性能。结果表明:该催化剂具有良好的活性和选择性;甲醇为反应的良溶剂;D3520载体对活性组份具有良好的吸附性能,延长了催化剂的使用寿命。     

高效液相色谱法分离和测定2,6-二特丁基对甲酚和2-特丁基对甲酚

1引宫2,6H持了基对甲酚和｝特丁基对甲酚为2种通用型酚类抗氧剂。它们对热、氧和老化有一定的防护作用。特别是2,＊二特丁基对甲酚,其用途更为广泛,可作聚乙烯、聚氯乙烯及聚乙烯基酸等的稳定剂,作合成橡胶常用的防老剂,石油产品的抗氧添加剂,食品加工工业用的抗氧剂。2．特丁基对甲酚除作抗氧剂外,还是很好的阻燃剂。2,6H特了基对甲酸和2．特了基对甲酚都是在催化剂存在下,由对甲苯酚与异丁烯或异丁醇进行烷基化反应而得到的,由于反应条件的不同,而分别生成这两种不同的产物。如果反应条件控制得不好,很可能在生成其中一种主…     

双波长紫外分光光度法测定混合甲酚中对甲酚和间甲酚的含量

本研究采用双波长紫外分光光度法对混合甲酚溶液中对甲酚和间甲酚的含量进行了测定。通过等吸光点的方法寻求最佳的波长对,获得了较高的测量灵敏度和准确度,用本法测定混合试样中间甲酚的含量,相对偏差小于1.5％;测定对甲酚的含量,相对偏差小于2.1％。     

对羟基苯甲醛的液相催化氧化合成

研究了活性炭负载磺化酞菁钴催化氧化对甲酚合成对羟基苯甲醛（ＰＨＢ）的诸多影响因素，筛选到较好的反应条件：反应时间，１２小时；温度，６０℃；ＮａＯＨ／对甲酚（ｍｏｌ比）为３．５∶１；催化剂，１５０ｐｐｍ；对甲酚的转化率，９７％；ＰＨＢ收率，８２．５％；选择性，８５．１％。     

对甲酚的气相色谱分析

建立了一种快速、准确测定了高纯度对甲酚的气相色谱分析方法，分别使用毛细管柱和填充柱对高纯度对甲酚及其异构体进行定量分析，所得结果与ＩＳＯ结晶点法完全一致。     

邻甲酚液相原位加氢反应

以Ni/CMK-3为催化剂,采用BET比表面积、X射线衍射和氢气程序升温还原对催化剂进行了表征.考察了不同Ni负载量、反应温度、反应初始压力及反应时间条件下,甲醇水相重整制氢与邻甲酚原位加氢的耦合反应.结果表明,当Ni负载量为20%、反应温度为230℃、反应前冷压为0.1 MPa、水-甲醇-模型化合物摩尔比为50∶15∶1及反应9 h时,邻甲酚转化率最高为45.4%.分别对比了甲醇、甲酸、甘油和异丙醇作为供氢溶剂对原位加氢反应的影响,其中以甲酸为供氢溶剂时,邻甲酚的转化率最高达82.2%.对比了甲酚3种同分异构体原位加氢的效果,发现邻甲酚和间甲酚的反应效果相差不大,而对甲酚的转化率则远低于邻甲酚和间甲酚.对20%Ni/CMK-3在原位加氢实验中的使用寿命进行了考察.     

柱前衍生高效液相色谱法分离分析甲酚异构体

提出了柱前衍生高效液相色谱法同时分离测定邻甲酚、间甲酚和对甲酚的方法。含甲酚异构体的样品与衍生化试剂按1比8(质量比)混合,加热回流衍生2 h。3种异构体的转化率依次为98.1%,99.0%,98.5%。选用Eclipse XDB-C_(18)色谱柱作为反相色谱柱,以甲醇和水以体积比为35比65的混合溶液为流动相,在260nm波长处进行测定,乙酸邻甲酚酯、乙酸间甲酚酯的峰面积与其浓度在(0.05～3.75)×10~(-5)mol·L~(-1)范围内呈线性关系,而乙酸对甲酚酯在(0.03～2.25)×10~(-5)mol·L~(-1)之间呈线性关系,检出限(3S/N)依次为1.88×10~(-5),1.88×10~(-5),1.13×10~(-5)mol·L~(-1)。此方法应用于实际样品的测定,回收率分别为104%,95%,100%,相对标准偏差(n=7)分别为0.22%,2.34%,0.90%。     

常压下由对甲酚催化氢化制备4—甲基环己酮

4-甲基环己酮作为一种优良的有机溶剂及有机合成中间体,在微电子工业及医药、香料、精细化工合成中有很重要的用途。文献报道的各种制备方法中,以对甲酚为原料经催化氢化制备4-甲基环己酮有实际意义。但催化氢化大多在加压情况下进行,所用催化剂多为钯,也有用钉、铑或莱尼镍作催化剂的,但加氢产物多为甲基环己醇,且酮的收率很低。本文采用铑催化剂(以氧化铝作载体),实现了对甲酚的常压催化氢化,制得4-甲基环己酮,并对催化条件作了初步摸索和探讨。     

FeZSM-5/N2O体系催化氧化甲苯制甲酚的研究

采用四丙基氢氧化铵为模板剂, 硝酸铁为铁源应用水热合成法制备了一系列FeZSM-5分子筛催化剂, 利用X-射线粉末衍射分析, N2吸附/脱附, 元素分析等技术对催化剂进行了表征. 并进行了所制样品对甲苯催化氧化制甲酚反应催化性能的研究. 本文详细考察了Fe含量、反应物配比、反应温度以及空速等各种因素对甲苯催化氧化制甲酚反应催化性能的影响. 结果表明在400 ℃, 甲苯∶N2O为1∶4, 空速为8 000 mL·h-1·g-1条件下反应结果最佳, 最大甲苯转化率约为12.6%, 甲酚选择性约为33.0%.     

煤焦油中酚类物质对焦油组分加氢脱氮脱硫以及芳烃饱和的影响

在固定床加氢微反装置上,考察了邻甲酚对煤焦油组分喹啉加氢脱氮(HDN)反应、二苯并噻吩(DBT)加氢脱硫(HDS)反应以及1-甲基萘加氢饱和(HDA)反应的影响。结果表明,邻甲酚的加入对喹啉的HDN反应、DBT的HDS反应、1-甲基萘的HDA反应有着较强的抑制作用,且邻甲酚的含量越多,这种抑制作用越明显,这是由于邻甲酚与喹啉、DBT、1-甲基萘在活性位点上的竞争吸附造成的。邻甲酚的加入对产物的选择性影响较弱,反应前后产物的选择性变化很小。由于空间位阻效应,1-甲基萘的加氢优先发生在不带侧链的芳环上。     

Electrolysis of Nitric Acid by Using a Glassy Carbon Fiber Column Electrode System

The electrochemical redox behavior of nitric acid was studied using a glassy carbon fiber column electrode system, and its reaction mechanism was suggested and confirmed in several ways. Electrochemical reactions in less than 2.0M nitric acid was not observed. However, in more than 2.0M nitric acid, the reduction of nitric acid to nitrous acid occurred and the reduction rate was slow so that the nitric acid solution had to be in contact with an electrode for a period of time long enough for an apparent reduction current of nitric acid to nitrous acid to be observed. The nitrous acid generated in more than 2.0M nitric acid was rapidly and easily reduced to nitric oxide by an autocatalytic reaction. Sulfamic acid was confirmed to be effective to destroy the nitrous acid. At least 0.05M sulfamic acid was necessary to scavenge the nitrous acid generated in 3.5M nitric acid.     

铅与硝酸反应及影响因素

铅与硝酸的反应比较复杂,在无机化学教材和相关资料中对铅与硝酸反应的阐述不一致,这将不利于学生在无机化学学习中对铅的基本性质的掌握。针对无机化学教材中存在的问题,本文通过大量实验探究了铅与硝酸反应的条件以及硝酸浓度、反应温度、反应时间等对铅与硝酸反应的影响,并考查了硝酸铅在不同浓度硝酸中溶解度的变化,利用红外光谱(IR)和X射线粉末衍射(XRD)对铅与浓硝酸的反应产物进行了表征,明确了铅易溶于稀硝酸而在浓硝酸中溶解度小的实质。     

Verteilung von Säure,Wasser, Methanol, Äthanol und Aceton Zwischen Gemischt Wässrig-Organischen Salpetersäurelösungen und Lösungen von Trilaurylammoniumnitrat in Cyclohexan

The distribution of acid, water, methanol, ethanol and acetone between mixed aqueous-organic nitric acid solutions and solutions of trilaurylammoniumnitrate in cyclohexane has been investigated. The distribution of acid rises with increasing concentrations of nitric acid, methanol, ethanol and acetone in the mixed aqueous-organic phase. The effect of the organic additives in increasing the distribution of the acid is methanol<ethanol<acetone. The concentration of nitric acid in the organic phase can be calculated by a formula similar to that describing the extraction from pure aqueous solutions. The distribution curves of water, methanol and ethanol resemble each other, all of them showing a minimum, when the distribution ration is plotted versus the nitric acid concentration in the mixed aqueous-organic phase. The acetone distribution decreases steadily with increasing nitric acid concentration. The shape of the curves is briefly discussed.      

Estimation of metal impurities in high-purity nitric acids used for metal analysis by inductively coupled plasma-mass spectrometry.

A simple method to estimate the amounts of ultra-trace metal impurities in nitric acid reagents has been developed. The determination of sixty-four metals in nitric acid was accomplished by direct measurements of 0.1 M nitric acids accurately diluted with ultrapure water by ICP-MS. Though accurate metal concentration could not be obtained for all of the elements, we could effectively evaluate the nitric acid quality by comparing the ion counts of the samples, ultrapure water and standard metal solutions for a calibration prepared with Ultrapur nitric acid.     

Component activities in the system thorium nitrate-nitric acid-water at 25°C

The equilibrium composition of the vapor above thorium nitrate-nitric acid-water mixtures has been studied as a function of the concentrations of thorium nitrate and nitric acid using a transpiration technique. At 25°C, the thorium nitrate concentrations m _T ranged from 0.1 to 2.5 molal and the nitric acid concentrations m _N from 0.3 to 25 modal. The vapor pressure of the nitric acid was found to increase with increasing thorium nitrate concentration for a constant molality of nitric acid in aqueous solution. At constant m _T , the nitric acid vapor pressure was particularly enhanced at low nitric acid concentrations. The water vapor pressures decreased regularly with increasing concentrations of both nitric acid and thorium nitrate. The experimental data were fitted to Scatchard's ion-component model, and to empirical multiparameter functions. From the fitting parameters, and available literature data for the nitric acid-water and thorium nitrate-water systems at 25°C, expressions were calculated for the variation of water and thorium nitrate activities, as functions of the nitric acid and thorium nitrate concentrations, using the Gibbs-Duhem equation. Calculated values for the thorium nitrate activities were strongly dependent on the form of the function originally used to fit the vapor pressure data.Issued as AECL-7461.     

The application of novel hydrophobic ionic liquids to the extraction of uranium(VI) from nitric acid medium and a determination of the uranyl complexes formed

Novel ammonium based hydrophobic ionic liquids (ILs) have been synthesised and characterised, and their use in the liquid-liquid extraction of uranium(VI) from an aqueous nitric acid solution using tri-n-butyl phosphate (TBP), studied. On varying the nitric acid concentration, each IL was found to give markedly different results. Relatively hydrophilic ILs showed high uranium(VI) extractability at 0.01 M nitric acid solution which progressively decreased from 0.01 to 2 M HNO(3) and then increased again as the nitric acid concentration was increased to 6 M. An analysis of the mechanisms involved for one such IL, pointed to cationic-exchange being the predominant route at low nitric acid concentrations whilst at high nitric acid concentrations, anionic-exchange predominated. Strongly hydrophobic ILs showed low extractability for nitric acid concentrations below 0.1 M but increasing extractability from 0.1 M to 6 M nitric acid. The predominant mechanism in this case involved the partitioning of a neutral uranyl complex. The uranyl complexes were found to be UO(2)(2+)·(TBP)(3) for the cationic exchange mechanism, UO(2)(NO(3))(2)(TBP)(2) for the neutral mechanism and UO(2)(NO(3))(3)(-)·(TBP) for the anionic exchange mechanism.     

电感耦合等离子体质谱(ICP-MS)法测定玻纤滤筒中金属元素本底值的预处理方法探讨

探讨了不同预处理方法对国产玻纤滤筒本底值的降低效果,便于废气样品的分析测定。分别对空白滤筒、热硝酸、硝酸+硫酸和硝酸+EDTA、HCl处理后的滤筒进行分析,测得滤筒中金属元素的含量;对处理效果较好的一批滤筒进行空白加标,考察加标回收率,全程用电感耦合等离子体质谱(ICPMS)法对样品进行测定,结果发现空白滤筒中部分金属元素含量较高;热硝酸处理后,滤筒本底中铅含量有所降低,但其它元素去除效果不显著;硝酸+硫酸处理后,滤筒中铅含量剧增;硝酸+EDTA处理滤筒,铅可以得到较好的去除效果,大部分金属元素含量有了明显降低;基于HCl对金属有较好的溶出效果,浸泡可较好地降低滤筒中金属元素的含量,但大量氯离子存在对ICP-MS法测定的干扰较大。对硝酸+EDTA处理后的滤筒进行空白加标,大部分金属元素加标回收率75%。故以硝酸+EDTA处理玻纤滤筒可以使国产玻纤滤筒适用于废气样品的分析。     

Extraction of copper(II) with the APCD/DIBK system from concentrated hydrochloric and nitric acid media: estimation of true limit of acidity for the extraction

The extraction of copper(II) from strongly acidic solution (0.01-8M hydrochloric and 0.01-5M nitric acid) with ammonium 1-pyrrolidinecarbodithioate in di-isobutyl ketone has been studied. Compared with the hydrochloric acid system, a considerably larger amount of the reagent is needed for complete extraction of copper chelate from nitric acid solution as the extract is more unstable in the nitric acid system. The decomposition of copper chelates extracted from nitric acid is based on the oxidation of the reagent and the chelate; the spectral change of the extract from nitric acid suggests that the copper(II) chelate is initially oxidized to copper(II) and then decomposes. The upper limit of the acidity of both acids from which the copper chelate can be quantitatively extracted strongly depends on the reagent concentration; the limit with 8 x 10(-2)M APCD (500-fold reagent: metal molar ratio) was taken as 8 and 4M for hydrochloric and nitric acid, respectively.     

Composition of phosphoric acid solutions obtained when orthophosphoric acid is used as solvent for iron-containing samples by heating: The influence of nitric acid, sulphuric acid and iron(III)

The dissolution of an iron-containing substance in orthophosphoric acid either alone or mixed with nitric acid or nitric acid-sulphuric acid mixture at 270-280 degrees has been examined, to determine the composition of the solutions which are used for analytical determinations. The possibility of condensation of H(3)PO(4) and formation of polyphosphoric acids during the dissolution has been proved. Solutions which may contain pyrophosphoric acid, tripolyphosphoric acid and tetrapolyphosphoric acid have been obtained. The exact composition of these solutions depends on the initial H(3)PO(4) concentration, the heating time, and, in some cases, the presence of nitric acid and sulphuric acid. It is assumed that the nitric and sulphuric acid affect the loss of water and therefore the thermal dehydration of the orthophosphoric acid during the dissolution. No qualitative changes in the phosphoric acid composition have been observed in the presence of Fe(III). Formation of Fe(III) polyphosphates is assumed.     

Extraction of uranium(VI) from nitric acid medium by 1.1M tri-n-butylphosphate in ionic liquid diluent

Summary A systematic study on the extraction of U(VI) from nitric acid medium by tri-n-butylphosphate (TBP) dissolved in a non-traditional diluent namely 1-butyl-3-methylimidazolium hexafluorophosphate (bmimPF₆) ionic liquid (IL) is reported. The results are compared with those obtained using TBP/n-dodecane (DD). The distribution ratio for the extraction of U(VI) from nitric acid by 1.1M TBP/bmimPF₆ increases with increasing nitric acid concentration. The U(VI) distribution ratios are comparable in the nitric acid concentration range of 0.01M to 4M, to the ratios measured using 1.1M TBP/DD. In contrast to the extraction behavior of TBP/DD, the D values continued to increase with the increase in the concentration of nitric acid above 4.0M. The stoichiometry of uranyl solvate extracted by 1.1M TBP/IL is similar to that of TBP/DD system, wherein two molecules of TBP are associated with one molecule of uranyl nitrate in the organic phase. Ionic liquid alone also extracts uranium from nitric acid, albeit to a small extent. The exothermic enthalpy accompanying the extraction of U(VI) in TBP/bmimPF₆ decreases with increasing nitric acid and with TBP concentrations.