微酸性条件下环己基过氧化氢分解制备环己酮工艺研究

针对传统碱性分解的不足,以有机铬酸酯为催化剂,对环己烷氧化液中的环己基过氧化氢分解制备环己酮工艺进行了探索,考察了在催化剂铬离子浓度150 ppm时,分解温度及时间对环己烷氧化液分解产物的影响,得出最佳的微酸性分解工艺条件.并在连续分解实验装置对前面得到的微酸性分解工艺条件进行验证.     

Formation of 4-arylpyridines from pyridinium salts under the action of methylammonium sulfite

Reactions of pyridinium salts or nonquaternized pyridine with 4-methylpyridinium salts in the presence of methylammonium sulfite in aqueous methylamine afford 4-phenylpyridine in 29—57% yields. The probable mechanism of ring transformation in simplest pyridine derivatives under the action of nucleophiles is discussed.     

Thermal studies on the sodium salts of aminosalicylic acids

The effect on the stability of the isomers of aminosalicylic acid of formation of their sodium salts has been studied by use of differential scanning calorimetry and thermogravimetry, coupled with evolved gas analysis by Fourier transform infrared spectroscopy. X-ray powder diffraction and infrared spectroscopy provided complementary information. The DSC curves for the sodium salts of all of the isomers showed complex dehydration/decomposition endotherms. From the initial mass losses of the TG curves, the amounts of water per mole of salt were estimated as 0.5, 2.4 and 1.4 moles for the sodium salts of 3-aminosalicylic acid, 4-aminosalicylic acid and 5-aminosalicylic acid, respectively. TG-FTIR results for the sodium salt of 3-aminosalicylic acid showed the evolution of carbon dioxide in three stages: below 150°C, between 200 and 300°C and continuous formation up to 500°C. This behaviour differs from that of 3-aminosalicylic acid itself, which forms CO₂ between 225 and 290°C. For the sodium salt of 4-aminosalicylic acid, the formation of carbon dioxide starts from 250°C and is still being formed at about 650°C. 4-aminosalicylic acid decarboxylates above 150°C. 5-aminosalicylic acid and its sodium salt showed no evolution of carbon dioxide below 600°C. This revised version was published online in July 2006 with corrections to the Cover Date.     

wo3催化h2o2氧化环己酮合成己二酸

以WO3为催化剂,在无有机溶剂和相转移催化剂的情况下,用H2O2氧化环己酮合成己二酸。探讨了催化剂用量、H2O2用量、反应温度和时间等条件对反应的影响。在优化条件下:n(环己酮)∶n(H2O2)∶n(WO3)=100∶500∶2,反应温度为120℃,反应6 h,己二酸分离收率可达80.3%,纯度为99.8%;催化剂重复使用5次后己二酸收率仍可达70.2%。     

钨化合物催化过氧化氢氧化环己酮合成己二酸

在无相转移催化剂的条件下,用Na2WO4·2H2O 或 H7[P(W2O7)6]·xH2O为催化剂,30% H2O2可以将环己酮高产率地氧化成己二酸.钨催化剂用量、反应液酸度对反应结果有着重要的影响.当钨原子与环己酮的摩尔比为1.5%,反应初始液的pH值为1.0时,己二酸的得率可达82%;而且催化体系具有很好的可循环性.     

钛硅分子筛催化环己酮液相氨肟化固定床工艺

采用固定床模式,研究了钛硅分子筛催化环己酮制环己酮肟液相氨肟化反应.结果表明,该工艺模式具有可行性与普适性.优化的反应条件为:温度333K,体系氨浓度>2%,酮/H₂O₂摩尔比=5,H₂O₂空速0.083h^-1.此时环己酮转化率、环己酮肟选择性、H₂O₂转化率及其有效利用率分别达18.7%,99.5%,94.7%和98.7%.进一步研究了H₂O₂在该过程中的反应行为,发现固定床工艺模式能有效提高H₂O₂的有效利用率,其主要原因是该模式有利于羟胺的生成及其进一步与酮反应生成肟.适当的空速与氨和酮的浓度是实现H₂O₂高效利用的关键因素.     

过氧杂多酸(盐)在催化有机反应中的应用

含活性氧的过氧杂多酸(盐)是由杂多酸(盐)与过量H2O2反应而生成的,其具有高效的催化活性,可以用于催化氧化不同的物质,是一类性能优异的绿色催化剂,其在有机合成中有十分广阔的发展前景。本文介绍了过氧杂多酸(盐)的结构、性质和催化作用,并综述了近年来其在催化有机反应中的研究进展。     

NaY型沸石分子筛催化环己胺氧化制备环己酮肟

考察了系列氧化剂、催化剂和溶剂对环己胺液相氧化制备环己酮肟的影响,发现以乙腈为溶剂,过氧化氢为氧化剂,NaY型沸石分子筛对该反应具有优良的催化性能。 对该反应体系进行了五因素四水平的正交实验,确定了适宜的催化剂用量、溶剂用量、反应时间、反应温度和氧化剂用量,比较分析了各因素对环己胺转化率和环己酮肟选择性的影响。 确定了环己胺液相氧化反应的最佳工艺条件为：环己胺为3 mL,催化剂为03 g,环己胺、溶剂和氧化剂的体积比为1∶3∶3,65 ℃反应2 h。 讨论了环己胺液相催化氧化的反应机理。     

Catalytic ring opening of acetylcyclopropane by water and alcohols under the action of copper or palladium salts

The possibility of the cleavage of the C—C bond in acetylcyclopropane (ACP) under the action of water or alcohols in the presence of copper or palladium salts was demonstrated for the first time. At 175—180 °C, the reactions proceeded regioselectively with the cleavage of the C(1)—C(2) bond in the cyclopropane ring. The reaction of ACP with water afforded 5-hydroxypentan-2-one, bis(3-acetylpropyl) ether, and furan compounds, whereas the reactions with alcohols proceeded selectively to form 5-alkoxypentan-2-ones. The yields of the latter depend on the nature and structure of the alcohol, the maximum values (98%) being achieved in the case of primary alcohols.     

Unexpected high oxidation of cyclohexane by Fe salts and dihydrogen peroxide in acetonitrile

The reaction of cyclohexane (CyH) with 1.5 equivalent of dihydrogen peroxide (30% aqueous solution) in the presence of 1 mol% of an iron(II) or iron(III) salt (without added ligand), at 50 °C in acetonitrile, produces cyclohexanol (CyOH) and cyclohexanone (CyO) in high yields (up to 87% of CyH is converted to CyOH + CyO). Remarkably, CyH is totally converted within 2 h in the presence of Fe(ClO₄)₂ as catalyst under argon, producing 45% of CyOH and 42% of CyO. The addition of a tridentate Schiff-base ligand, namely 2,6-bis-[1-(benzylimino)ethyl]pyridine (dapb), leads to a clear increase of the selectivity towards CyOH + CyO, which are obtained with an overall yield of 93% (and even 100% selectivity to CyOH and CyO) in the case of the [Fe(ClO₄)₃/dapb] catalytic system.     

Deuterium isotope effect on 13C chemical shifts of tetrabutylammonium salts of Schiff bases amino acids

Deuterium isotope effects on 13C chemical shift of tetrabutylammonium salts of Schiff bases, derivatives of amino acids (glycine, L-alanine, L-phenylalanine, L-valine, L-leucine, L-isoleucine and L-methionine) and various ortho-hydroxyaldehydes in CDCl3 have been measured. The results have shown that the tetrabutylammonium salts of the Schiff bases amino acids, being derivatives of 2-hydroxynaphthaldehyde and 3,5-dibromosalicylaldehyde, exist in the NH-form, while in the derivatives of salicylaldehyde and 5-bromosalicylaldehyde a proton transfer takes place. The interactions between COO- and NH groups stabilize the proton-transferred form through a bifurcated intramolecular hydrogen bond.     

环己酮氨肟化反应中TS-1催化剂的积炭失活

 采用连续淤浆反应器,在环己酮质量空速为6 h-1和温度为70 ℃的条件下,对 TS-1 催化剂上环己酮氨肟化制环己酮肟反应过程中的活性变化规律进行了考察,并用热重-差热分析、程序升温脱附、 N2物理吸附、程序升温氧化和傅里叶变换红外光谱等测试手段对不同运转时间及再生后的催化剂进行了表征. 结果表明,催化剂运转时间在60 h以内时活性稳定,然后迅速下降; 积炭是引起催化剂失活的主要原因. 催化剂表面的积炭主要沉积在 TS-1 的微孔内,含碳物种有两种类型: 易除炭存在于Ti中心附近,可在350 ℃下氧化除去; 难除炭沉积于强酸中心 Si-OH 处,需在700 ℃下才能除去. 催化剂失活前后的骨架结构未发生显著变化,经烧炭再生后活性可恢复到新鲜催化剂的水平.     

Functionallization of the δ-carbon atom by the ferrous ion induced decomposition of alkyl hydroperoxides in the presence of cupric salts

In the ferrous ion induced decomposition of alkyl hydroperoxides in the presence of cupric halides or pseudohalides, intramolecular functionalization, with ligand transfer from cupric salts to δ-carbon atom, is achieved.     

Dehydrogenation of 1,4-dihydropyridine derivatives by the action of hydroperoxides in the presence of metal salts

Conclusions Molybdenum, tungsten, vanadium, and other metal salt-catalyzed hydroperoxide oxidation is a convenient preparative method for the dehydrogenation of 1,4-dihydropyridines to pyridine bases.Translated from Izvestiya Akademii Nauk SSSR, Seriya Khimicheskaya, No. 3, pp. 670–671, March, 1972.     

Laboratory synthesis of ferrous bromide

A laboratory method is presented for the preparation of ferrous bromide by heating ferric bromide or its crystal hydrate in toluene or xylene at reflux for 3–4 h. The yield is quantitative. The FeBr₂ or⁵⁷FeBr₂ sample thereby obtained may be used in the synthesis of iron porphyrin complexes.Institute for Physicotechnical Research, Russian Academy of Sciences, 151034 Moscow. Translated from Izvestiya Akademii Nauk, Seriya Khimicheskaya, No. 8, pp. 1927–1928, August, 1992.     

HRGC separation of hydroperoxides formed during the photosensitized oxidation of (R)—(+)-Limonene

(R)—(+)-Limonene was photooxidized in the presence of Rose Bengal as catalyst. After TLC isolation, the hydroperoxides formed were separated directly by HRGC and analyzed by MS (El; Cl). Each hydroperoxide isomer was then isolated by HPLC for structure determination which after reduction of the HOO group with sodium borohydride was performed by ¹H-NMR and ¹³C-NMR. Six hydroperoxide isomers formed by oxidation of the endocyclic double bond were identified. The compounds eluted from the HRGC column in the following order (proportions are given in brackets) I (40.1%) (1S, 4R)-p-mentha-2, 8-diene 1-hydroperoxide; II (5.8%) (1R, 4R)-p-mentha-2, 8-diene 1-hydroperoxide; III (20.6%) (2R, 4R)-p-mentha-[1(7), 8]-diene 2-hydroperoxide; IV (8.5%) (2R, 4R)-p-mentha-6, 8-diene 2-hydroperoxide; V (4%) (2S, 4R)-p-mentha-6, 8-diene 2-hydroperoxide; and VI (21.0%) (2S, 4R)-p-mentha-[1(7), 8]-diene 2-hydroperoxide. Direct HRGC separation of the limonene hydroperoxides offers, inter alia, the possibility of determining their flavor qualities by HRGC/effluent sniffing.