会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 51. 发明专利
    • PRODUCTION OF MALEIC ANHYDRIDE
    • JPS6219578A
    • 1987-01-28
    • JP15729485
    • 1985-07-17
    • MITSUBISHI CHEM IND
    • OTAKE MASAYUKIMURAYAMA MASAYOSHI
    • C07D307/60B01J27/198
    • PURPOSE:To obtain safely and advantageously the titled substance without problems of reaction heat control, by oxidizing benzene in a gaseous phase by the use of a fluidized bed catalytic composition containing the first component having specific crystal structure and the second component of an amorphous vanadium-phosphorous type compound oxide, as active ingredients. CONSTITUTION:The aimed compound is obtained by oxidizing benzene in a gaseous phase by the use of a fluidized bed catalyst comprising a crystalline compound oxide containing vanadium and phosphorous, having characteristic X-ray diffraction peaks shown by the table, as the first component and an amorphous compound oxide containing vanadium and phosphorous as the second component, as a catalyst, more preferably a fluidized bed catalyst obtained by blending the catalyst with a proper carrier as the third component to form an aqueous slurry, subjecting the slurry to spray drying the calcining the prepared solid particles. The gaseous phase concentration of benzene is preferably about 0.1-10wt%, especially preferably about 0.2-5%. The reaction temperature is preferably 350-500 deg.C.
    • 52. 发明专利
    • PRODUCTION OF MALEIC ANHYDRIDE
    • JPS61251678A
    • 1986-11-08
    • JP9244485
    • 1985-04-30
    • MITSUBISHI CHEM IND
    • OTAKE MASAYUKIYAGI HIROSHI
    • C07D307/60B01J27/198C07B61/00
    • PURPOSE:To produce maleic anhydride in improved reaction selectivity and operation safety, etc., by catalytically oxidizing an aliphatic hydrocarbon in vapor phase using a V-P compound oxide catalyst in the presence of a specific amount of a sulfur compound. CONSTITUTION:Maleic anhydride is produced by the vapor-phase oxidization of a >=4C aliphatic hydrocarbon such as n-butane, butene, etc., with air, etc., in the presence of a vanadium-phosphorus compound oxide catalyst (e.g. an oxide produced by dissolving vanadium pentoxide in an aqueous medium and subjecting the resultant solution containing 4-valent vanadium ion to hydrothermal treatment at 110-250 deg.C in the presence of e.g. phosphoric acid and an inorganic reducing agent). The above process is carried out in the presence of a sulfur compound (e.g. alkanethiol, alkylsulfone, etc.) at a high concentration, i.e. >=4ppm, especially >=5ppm in terms of sulfur atom based on the weight of the aliphatic hydrocarbon used as a raw material. The autoxidation reaction can be suppressed without retarding the oxidization reaction of the hydrocarbon to maleic anhydride.
    • 54. 发明专利
    • Production of lactone
    • 生产Lactone
    • JPS61115079A
    • 1986-06-02
    • JP23587484
    • 1984-11-08
    • Mitsubishi Chem Ind Ltd
    • OTAKE MASAYUKIUSHIKUBO TAKASHIKAYOU ATSUSHI
    • C07D307/33B01J23/00B01J23/89C07B61/00C07D307/32
    • Y02P20/52
    • PURPOSE: To obtain the titled compound in high selectivity without preparing by-products, by reacting a dicarboxylic acid with hydrogen by the use of a catalyst comprising palladium, chromium, and cobalt.
      CONSTITUTION: A dicarboxylic acid or its anhydrid is reacted with hydrogen in the presence of a catalyst containing palladium, chromium, and cobalt as essential components in the absence of a solvent or in a solvent such as a lactone, tetrahydrofuran, etc., to give a lactone. The catalyst used is usually obtained by preparing previously cobalt chromate from raw material compounds of a chromium component and a cobalt component, and adding a palladium component to it. An atomic ratio of palladium to chromium is 1/2,000W1/10, prefferably 1/1,1000W1/10,and an atomic ratio of cobalt to chromium is 1/10W10. maleic anhydride, succinic anhydride, etc., may be used as the dicabroxylic acid or its anhydride.
      COPYRIGHT: (C)1986,JPO&Japio
    • 目的:通过使用包含钯,铬和钴的催化剂使二羧酸与氢反应,以高选择性得到标题化合物而不制备副产物。 构成:在不存在溶剂的情况下或在溶剂如内酯,四氢呋喃等中,在含有钯,铬和钴的催化剂的存在下,二羧酸或其无水物与氢反应,得到 内酯。 所使用的催化剂通常通过从铬组分和钴组分的原料化合物制备预先的铬酸铬,并向其中加入钯组分来获得。 钯与铬的原子比为1 / 2,000-1 / 10,优选为1 / 1,1000-1 / 10,钴与铬的原子比为1/10〜10。 马来酸酐,琥珀酸酐等可以用作二十八酸或其酸酐。
    • 55. 发明专利
    • Zeolite composition
    • 沸石组合物
    • JPS6177620A
    • 1986-04-21
    • JP19980084
    • 1984-09-25
    • Mitsubishi Chem Ind Ltd
    • OTAKE MASAYUKITSURITA YASUSHI
    • C07C2/86B01J29/00C01B37/04C01B39/04C01B39/06C01B39/38C07B61/00C07C1/00C07C15/08C07C67/00
    • Y02P20/52
    • PURPOSE: To obtain a zeolite compsn. useful as a novel catalyst by allowing an aq. mixture contg. sparingly water-soluble alumina source, silica source, and phosphate source, together with org. amine or quat. ammonium ion to cause hydrothermal reaction.
      CONSTITUTION: An aq. mixture contg. sparingly water-soluble alumina source, silica source, and phosphate source together with an org. amine or a quat. ammonium ion is prepd. The aq. mixture is charged in an autoclave and heated to cause hydrothermal reaction. Crystalline aluminophospho silicate is obtd. by filtering the reaction liquid. The principal powder X-ray diffraction peaks of the zeolite compsn. are given in Table 1 and 2. The zeolite compsn. is suited as catalyst for reactions requiring shape selectivity, such as prepn. of dialkyl benzene compds., synthesis of hydrocarbon from methanol, etc.
      COPYRIGHT: (C)1986,JPO&Japio
    • 目的:获得沸石组合物。 通过使一种水溶液作为新型催化剂起作用。 混合物 少量水溶性氧化铝源,二氧化硅源和磷酸盐源,以及组织。 胺或季铵盐。 铵离子引起水热反应。 构成: 混合物 微溶水氧化铝源,二氧化硅源和磷酸盐源与组织。 胺或季铵盐。 铵离子是制备的。 水。。 将混合物装入高压釜中并加热以引起水热反应。 结晶硅铝硅酸盐是可以得到的。 通过过滤反应液。 沸石的主要粉末X射线衍射峰。 表1和表2给出了沸石。 适用于需要形状选择性的反应的催化剂,如制备。 的二烷基苯化合物,从甲醇中合成烃等
    • 56. 发明专利
    • METHOD FOR ISOMERIZING DIALKYLNAPHTHALENE
    • JPH06122635A
    • 1994-05-06
    • JP25012992
    • 1992-09-18
    • MITSUBISHI CHEM IND
    • OTAKE MASAYUKIMASUYAMA TETSUONAKANISHI AKIO
    • B01J29/08C07B61/00C07C5/27C07C15/24
    • PURPOSE:To efficiently isomerize a dialkylnaphthalene or its isomer mixture into a desired dialkylnaphthalene isomer in a short time, while preventing the loss of the dialkylnaphthalene or its isomer mixture due to side reactions such as a disproportionation reaction and a transalkylation reaction. CONSTITUTION:At least one kind of dialkylnaphthalene isomer is heated in the presence of a catalyst comprising faujasite type zeolite belonging to a hexagonal crystal group and preferably in the presence of hydrogen gas to isomerize the dialkylnaphthalene. Since the intergroup isomerization of the dialkylnaphthalenes is more apt to occur by raising the reaction temperature, increasing the concentration of the catalyst and prolonging the catalyst contact time, the reaction temperature is 100-400 deg.C, preferably 150-250 deg.C, for the intragroup isomerization, and is 200-500 deg.C, preferably 300-450 deg.C, for the intergroup isomerization. The catalyst is prepared by using the compounds for ordinary synthetic zeolite as a silica source and an alumina source and using 18- crown-6(1,4,7,10,13,16-hexaoxoacyloctadecane) as a template agent.
    • 60. 发明专利
    • PRODUCTION OF 2,6-DIALKYLNAPHTHALENE
    • JPH04112840A
    • 1992-04-14
    • JP23270090
    • 1990-09-03
    • MITSUBISHI CHEM IND
    • OTAKE MASAYUKIMASUYAMA TETSUONAKANISHI AKIO
    • B01J20/18B01J20/281C07B61/00C07C5/27C07C6/12C07C7/12C07C15/24
    • PURPOSE:To produce the subject compound by separating the 2,6-isomer from a feedstock oil containing a dialkylnaphthalene isomer mixture, subjecting the residual feedstock oil to converting reaction, raising the concentration of the 2,6-isomer, removing part, etc., of the 1,8-isomer fraction from the resultant reaction product and recycling the obtained dialkyl derivative to the initial step. CONSTITUTION:A feedstock oil containing a dialkylnaphthalene isomer mixture is brought into contact with Y-type zeolite preferably subjected to ion exchange with La, Ba, etc., to separate and obtain the 2,6-isomer. The resultant feedstock oil at a reduced 1,6-isomer concentration is then subjected to converting reaction in the presence of a solid acid catalyst or a Lewis acid catalyst in the vapor or the liquid phase at 20-500 deg.C under atmospheric pressure to 50 atm to raise the 2,6-isomer concentration. The obtained reaction product is subsequently fed to a distillation column to distill away low-boiling substances from the column top. Bottom liquids are then distilled to distill away the 1,8-isomer together with highboiling substances from the column bottom to the outside of the system. A dialkyl derivative obtained from the column top is then recycled to the initial step. As a result, operation can be smoothly performed by removing the 1,8-isomer.