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    • 2. 发明授权
    • Process for halogenation of aldehydes and production of oximes therefrom
    • 醛的卤化和肟的生产方法
    • US4155933A
    • 1979-05-22
    • US894870
    • 1978-04-10
    • John H. BonfieldAndiappan K. MurthyDonald Pickens
    • John H. BonfieldAndiappan K. MurthyDonald Pickens
    • C07C45/00C07C45/63C07C47/14C07C67/00C07C313/00C07C319/20C07C323/47C07C131/00
    • C07C45/63
    • In the halogenation under reflux conditions of an unhalogenated aldehyde of the formula ##STR1## with Cl.sub.2, Br.sub.2 or I.sub.2, the aldehyde and halogen are continuously fed into a reactor at a molar ratio of halogen to unhalogenated aldehyde between about 0.8:1 and about 1.1:1 and water is continuously fed into the unhalogenated reactor at a rate of between about 1% and about 20% by weight of aldehyde. The product .alpha.-haloaldehyde is thiohydrocarbylated and then oximated to form a 2-hydrocarbylthioaldoxime of the formula ##STR2## with improved yield and quality because of the improved yield and quality of unhalogenated .alpha.-haloaldehyde. An exemplary process includes the chlorination of isobutyraldehyde (IBA) to form .alpha.-chloroisobutyraldehyde (CIBA), the thiomethylation of CIBA to form 2-methyl-2 methylthio-propionaldehyde (MTIBA) and the oximation of MTIBA to form 2-methylthio-propionaldehyde oxime (aldicarb oxime or ADO).
    • 在式Cl 1,Br 2或I 2的未卤化醛的回流条件下,将醛和卤素以约0.8:1至约1.1的卤素与非卤化醛的摩尔比连续进料到反应器中 :1和水以醛的约1重量%至约20重量%的速率连续进料到未卤化反应器中。 产物α-卤代烃被硫代烃基化,然后氧化形成式“IMAGE”的2-烃基硫代醛肟,其产率和质量得到改善,因为改善了产生和质量的非卤代α-卤代醛。 一个示例性的方法包括异丁醛(IBA)氯化以形成α-氯异丁醛(CIBA),CIBA的甲硫基化形成2-甲基-2-甲硫基 - 丙醛(MTIBA)和肟化MTIBA以形成2-甲硫基 - 丙醛肟 (涕灭威肟或ADO)。
    • 3. 发明授权
    • Vapor phase synthesis of hexafluoroisobutylene
    • US4705904A
    • 1987-11-10
    • US820896
    • 1986-01-17
    • John H. BonfieldHarry E. Ulmer
    • John H. BonfieldHarry E. Ulmer
    • C07C17/26C07C45/58C07D303/48
    • C07D303/48C07C17/26C07C45/58
    • A vapor phase synthesis of hexafluoroisobutylene, which comprises contacting in the vapor phase in a catalyst zone, B, of a reactor hexafluoropropylene oxide with a fluorinated catalyst such as fluorinated silica-alumina at a temperature of about 400.degree.-600.degree. C. for a residence time sufficient to form a vapor stream comprising hexafluoroacetone which is thereafter directly contacted in a heating zone of the reactor with a vapor stream comprising a keytone-generating compound such as acetic anhydride at a temperature of about 500.degree.-700.degree. C. for a residence time sufficient to form a stream comprising hexafluoroisobutylene, substantially-free of perfluoroisobutylene and recovering the hexafluoroisobutylene product is disclosed. A direct one reactor vapor phase synthesis of hexafluoroisobutylene which comprises (a) contacting, in the vapor phase, hexafluoropropene with less than a stoichiometric amount of oxygen required to convert substantially all the hexafluoroisopropene into hexafluoropropylene oxide in the presence of a fluorinated catalyst such as fluorinated silica-alumina at a temperature of about 400.degree.-600.degree. C. for a time sufficient to form a vapor stream comprising hexafluoropropylene oxide substantially-free of oxygen; (b) directly contacting said vapor stream, in a catalyst zone, B, containing a fluorinated catalyst which is preferably the same as used in catalyst zone, A, at a temperature of about 400.degree.-650.degree., preferably about 500.degree.-650.degree. C. for a time sufficient to form a vapor stream comprising hexafluoroacetone; (c) directly contacting the vapor stream comprising hexafluroacetone with a vaporized compound such as acetic anhydride at a temperature of about 500.degree.-700.degree. C., preferably about 600.degree. C. for a time sufficient to form a vapor stream comprising hexafluoroisobutylene, substantially-free of perfluoroisobutylene; and (d) recovering hexafluoroisobutylene is also disclosed.
    • 5. 发明授权
    • Method of preparing formaldoxime trimer
    • 制备甲醛肟三聚体的方法
    • US4680394A
    • 1987-07-14
    • US778935
    • 1985-09-23
    • John H. Bonfield
    • John H. Bonfield
    • C07D251/06
    • C07D251/06
    • An improved process for preparing formaldoxime trimer is provided in which loss of the product is minimized and the prior art problems of long retention times to afford precipitation of the trimer which is difficult to filter and which occludes the undesirable salt of the acid that is difficult to remove. The method disclosed involved oximation of paraformaldehyde using dehydroxylamine sulfate and ammonia gas followed by steam stripping to recover formaldoxime and separate trimerization thereof followed by filtration recovery and drying.The formaldoxime trimer is produced in essentially quantitative yield and proceeds specifically by a procedure of steam stripping out the formaldoxime monomer from the synthesis liquor and allowing separate trimer formation and recovery. The product is free from inorganic salts and the mother liquor with formaldoxime monomer content, resulting from its recovery by filtration, does not represent a yield loss in that it is recyclable to the next synthesis reaction.
    • 提供了一种制备甲醛肟三聚体的改进方法,其中产物的损失最小化,并且现有技术的长保留时间问题使得三聚物沉淀难以过滤,并且阻断了不希望的酸的不希望的盐难以 去掉。 所公开的方法包括使用脱羟胺硫酸铵和氨气肟化多聚甲醛,然后蒸汽汽提以回收甲醛肟并分离其三聚,然后过滤回收和干燥。 形式肟三聚体以基本上定量的产率产生,并且通过从合成液中蒸出甲醛肟单体并允许分离的三聚体形成和回收的方法进行具体实施。 该产物不含无机盐,由过氧化还原产生的甲醛肟单体含量的母液不代表产率损失,因为它可以回收下一个合成反应。