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    • 2. 发明授权
    • Method for producing maleic anhydride
    • US07087767B2
    • 2006-08-08
    • US10522993
    • 2003-07-22
    • Jens WeigunyWilhelm RuppelMark Duda
    • Jens WeigunyWilhelm RuppelMark Duda
    • C07D307/60
    • C07D307/60
    • Process for preparing maleic anhydride by heterogeneously catalyzed gas-phase oxidation of hydrocarbons having at least four carbon atoms by means of oxygen-containing gases at from 350 to 500° C. in the presence of a volatile phosphorus compound over a vanadium-, phosphorus- and oxygen-containing catalyst in a shell-and-tube reactor unit having at least one reaction zone cooled by means of a heat transfer medium, in which the temperature and/or the amount of the heat transfer medium flowing into the first (relative to the feed direction) reaction zone are set so that the mean temperature of the heat transfer medium in the first reaction zone TSB(1st zone), which is calculated as the mean of the inflow temperature and the outflow temperature of the heat transfer medium, is in accordance with the formulae (I) and (II) TSB(1st zone)≦TR(1st zone)−TSafety(1st zone)  (I) TSB, Ymax(1st zone)−TA(1st zone)≦TSB(1st zone)≦TSB, Ymax(1st zone)+TB(1st zone),  (II) where TR(1st zone) is the runaway temperature of the first reaction zone; TSafety(1st zone) is the safety temperature of the first reaction zone and has a value of 1° C.; TSB, Ymax(1st zone) is the mean temperature of the heat transfer medium in the first reaction zone at which the maximum maleic anhydride yield is achieved in the range TSB(1st zone)≦TR(1st zone); TA(1st zone) is 20° C.; and TB(1st zone) is 10° C.
    • 4. 发明授权
    • Process for the preparation of halobenzaldehydes
    • 卤代苯甲醛的制备方法
    • US5648551A
    • 1997-07-15
    • US592069
    • 1996-01-26
    • Holger BorchertThomas GerdauJens Weiguny
    • Holger BorchertThomas GerdauJens Weiguny
    • B01J23/847B01J23/85B01J23/88C07B61/00C07C45/36C07C47/55
    • C07C45/36
    • The invention relates to a process for the preparation of halobenzaldehydes of the formula (I): ##STR1## in which Hal is fluorine, chlorine, bromine or iodine and z=1, 2, 3 or 4, by catalytic gas-phase oxidation of a substituted toluene of the formula (II), ##STR2## by oxygen, which comprises carrying out the oxidation in the presence of a catalyst of the formula (III)Me.sup.1.sub.a Me.sup.2.sub.b Me.sup.3.sub.c O.sub.x (III),in which Me.sup.1 is bismuth or vanadium, Me.sup.2 is at least one of the elements selected from the group consisting of lithium, sodium, potassium, rubidium and cesium, Me.sup.3 is at least one element selected from the group consisting of iron, cobalt, nickel, niobium, molybdenum, arsenic, tin, antimony, tungsten, tantalum, phosphorus, chromium, manganese, palladium, copper, zinc, cerium, silver, boron, samarium, barium, calcium, magnesium and rhenium, and the letters a, b and c represent an atomic ratio of the respective elements such that when a=1, b has a value in the range from 0.1 to 2 and c has a value in the range from 0.05 to 2, different values for b and c being possible for different elements Me.sup.2 or Me.sup.3.
    • 本发明涉及一种制备式(I)的卤代苯甲醛的方法:其中Hal是氟,氯,溴或碘,z = 1,2,3或4,通过催化气 - 其中包括在式(III)Me1aMe2bMe3cOx(III)的催化剂存在下进行氧化,其中Me1是铋(III),式(II)的取代的甲苯, 或钒,Me 2是选自锂,钠,钾,铷和铯中的至少一种元素,Me 3是选自铁,钴,镍,铌,钼,砷中的至少一种元素 锡,锑,钨,钽,磷,铬,锰,钯,铜,锌,铈,银,硼,钐,钡,钙,镁和铼,字母a,b和c表示 各个元件使得当a = 1时,b具有在0.1至2的范围内的值,c具有值 在0.05至2的范围内,对于不同的元素Me2或Me3,b和c的不同值是可能的。
    • 6. 发明申请
    • PROCESS FOR OBTAINING MALEIC ANHYDRIDE BY DISTILLATION
    • 通过蒸馏获得马来酸酐的方法
    • US20100113805A1
    • 2010-05-06
    • US12532660
    • 2008-03-19
    • Gunther WindeckerGerd KaibelMichael SteinigerThilo BuntrockJens WeigunyDany Vanden HautteThierry Lurquin
    • Gunther WindeckerGerd KaibelMichael SteinigerThilo BuntrockJens WeigunyDany Vanden HautteThierry Lurquin
    • C07D307/60
    • B01D3/14B01D3/141C07C51/573C07C57/145
    • What is described is a process for obtaining maleic anhydride by distillation from a solution of maleic anhydride in a high-boiling absorbent which has been obtained by gas phase oxidation of a hydrocarbon and at least partial absorption of the oxidation products into the absorbent, by i) introducing the solution into the side of a feed column with a rectifying section disposed above the feed point and a stripping section disposed below the feed point, ii) providing an upper combining column which communicates with the upper end of the rectifying section and a lower combining column which communicates with the lower end of the stripping section, iii) providing a draw column which communicates with the upper combining column and the lower combining column, iv) drawing maleic anhydride off as a side draw from the draw column, and drawing off compounds having a lower boiling point than maleic anhydride at the top of the upper combining column and the high-boiling absorbent at the bottom of the lower combining column. The maleic anhydride obtained as a side draw has a low content of acrylic acid and acetic acid.
    • 所描述的是通过蒸馏从马来酸酐在高沸点吸收剂中的溶液获得马来酸酐的方法,其通过烃的气相氧化和至少部分吸收氧化产物进入吸收剂中获得, 将溶液引入进料塔的侧面,其中设置在进料点上方的精馏部分和设置在进料点下方的汽提部分,ii)提供与精馏部分的上端连通的上部混合塔和下部 组合柱与汽提部分的下端连通,iii)提供与上部混合塔和下部混合塔连通的牵引柱,iv)将拉伸马来酸酐作为拉伸塔的牵引拉出,拉出 在上部混合塔的顶部具有比马来酸酐低的沸点的化合物和在底部o的高沸点吸收剂 f下组合列。 作为侧馏分获得的马来酸酐具有低含量的丙烯酸和乙酸。
    • 8. 发明授权
    • Process for obtaining maleic anhydride by distillation
    • 通过蒸馏获得马来酸酐的方法
    • US08461356B2
    • 2013-06-11
    • US12532660
    • 2008-03-19
    • Gunther WindeckerGerd KaibelMichael SteinigerThilo BuntrockJens WeigunyDany Vanden HautteThierry Lurquin
    • Gunther WindeckerGerd KaibelMichael SteinigerThilo BuntrockJens WeigunyDany Vanden HautteThierry Lurquin
    • C07D307/36
    • B01D3/14B01D3/141C07C51/573C07C57/145
    • What is described is a process for obtaining maleic anhydride by distillation from a solution of maleic anhydride in a high-boiling absorbent which has been obtained by gas phase oxidation of a hydrocarbon and at least partial absorption of the oxidation products into the absorbent, by i) introducing the solution into the side of a feed column with a rectifying section disposed above the feed point and a stripping section disposed below the feed point, ii) providing an upper combining column which communicates with the upper end of the rectifying section and a lower combining column which communicates with the lower end of the stripping section, iii) providing a draw column which communicates with the upper combining column and the lower combining column, iv) drawing maleic anhydride off as a side draw from the draw column, and drawing off compounds having a lower boiling point than maleic anhydride at the top of the upper combining column and the high-boiling absorbent at the bottom of the lower combining column. The maleic anhydride obtained as a side draw has a low content of acrylic acid and acetic acid.
    • 所描述的是通过蒸馏从马来酸酐在高沸点吸收剂中的溶液获得马来酸酐的方法,其通过烃的气相氧化和至少部分吸收氧化产物进入吸收剂中获得, 将溶液引入进料塔的侧面,其中设置在进料点上方的精馏部分和设置在进料点下方的汽提部分,ii)提供与精馏部分的上端连通的上部混合塔和下部 组合柱与汽提部分的下端连通,iii)提供与上部混合塔和下部混合塔连通的牵引柱,iv)将拉伸马来酸酐作为拉伸塔的牵引拉出,拉出 在上部混合塔的顶部具有比马来酸酐低的沸点的化合物和在底部o的高沸点吸收剂 f下组合列。 作为侧馏分获得的马来酸酐具有低含量的丙烯酸和乙酸。
    • 9. 发明授权
    • Catalyst-precursor for the production of maleic acid anhydride and method for the production thereof
    • 用于生产马来酸酐的催化剂前体及其制备方法
    • US07169732B2
    • 2007-01-30
    • US10507610
    • 2003-03-12
    • Jens WeigunySebastian StorckMark DudaCornelia Dobner
    • Jens WeigunySebastian StorckMark DudaCornelia Dobner
    • B01J27/18C07D307/60
    • C07C51/252B01J23/002B01J27/198B01J35/002B01J35/1014B01J37/0018B01J37/031B01J2523/00C07C51/215C07C57/145B01J2523/51B01J2523/55
    • A process for preparing a vanadium, phosphorus, and oxygen catalyst precursor for preparing maleic anhydride by heterogeneously catalyzed gas-phase oxidation of a hydrocarbon having at least four carbon atoms, which comprises (a) reacting vanadium pentoxide with from 102 to 110% strength phosphoric acid in the presence of a primary or secondary, noncyclic or cyclic, unbranched or branched, saturated alcohol having from 3 to 6 carbon atoms in a temperature range from 80 to 160° C.; (b) isolating the precipitate formed; (c) setting an organic carbon content of ≦1.1% by weight in the isolated precipitate by heat treatment in a temperature range from 250 to 350° C., the heat-treated product, following the addition of 3.0% by weight of graphite, giving a powder X-ray diffraction diagram which in the 2θ region features a ratio of the height of the peak of any pyrophosphate phase present at 28.5° to the height of the peak due to the graphite at 26.6° of ≦0.1; and (d) shaping the heat-treated product obtained from step (c) into particles having an averaged diameter of at least 2 mm; a catalyst precursor obtainable from this process; a process for preparing a catalyst from the catalyst precursor; a catalyst obtainable from that process; and also a process for preparing maleic anhydride over that catalyst.
    • 一种制备用于通过异构催化气相氧化具有至少四个碳原子的烃来制备马来酸酐的钒,磷和氧催化剂前体的方法,其包括(a)使五氧化二钒与102-110%强度的磷酸 在80至160℃的温度范围内在具有3至6个碳原子的伯或仲,非环或环状,无支链或支链的饱和醇存在下进行酸反应。 (b)分离形成的沉淀物; (c)通过在250-350℃的温度范围内通过热处理将分离的沉淀物中的有机碳含量<= 1.1重量%设定为热处理产物,添加3.0重量%的石墨 ,给出粉末X射线衍射图,其在2θ区域的特征是存在于28.5°的任何焦磷酸盐相的峰的高度与由于石灰在26.6°<= 0.1处的峰的高度之比; 和(d)将由步骤(c)获得的热处理产物成型为具有至少2mm的平均直径的颗粒; 从该方法获得的催化剂前体; 从催化剂前体制备催化剂的方法; 可从该方法获得的催化剂; 以及在该催化剂上制备马来酸酐的方法。
    • 10. 发明申请
    • Method for producing maleic anhydride
    • US20050256319A1
    • 2005-11-17
    • US10522993
    • 2003-07-22
    • Jens WeigunyWilhelm RuppelMark Duda
    • Jens WeigunyWilhelm RuppelMark Duda
    • C07B61/00C07D307/60C07D307/36
    • C07D307/60
    • Process for preparing maleic anhydride by heterogeneously catalyzed gas-phase oxidation of hydrocarbons having at least four carbon atoms by means of oxygen-containing gases at from 350 to 500° C. in the presence of a volatile phosphorus compound over a vanadium-, phosphorus- and oxygen-containing catalyst in a shell-and-tube reactor unit having at least one reaction zone cooled by means of a heat transfer medium, in which the temperature and/or the amount of the heat transfer medium flowing into the first (relative to the feed direction) reaction zone are set so that the mean temperature of the heat transfer medium in the first reaction zone TSB(1st zone), which is calculated as the mean of the inflow temperature and the outflow temperature of the heat transfer medium, is in accordance with the formulae (I) and (II) TSB(1st zone)≦TR(1st zone)−TSafety(1st zone)   (I) TSB, Ymax(1st zone)−TA(1st zone)≦TSB(1st zone)≦TSB, Ymax(1st zone)+TB(1st zone)   (II), where TR(1st zone) is the runaway temperature of the first reaction zone; TSafety(1st zone) is the safety temperature of the first reaction zone and has a value of 1° C.; TSB, Ymax(1st zone) is the mean temperature of the heat transfer medium in the first reaction zone at which the maximum maleic anhydride yield is achieved in the range TSB(1st zone)≦TR(1st zone); TA(1st zone) is 20° C.; and TB(1st zone) is 10° C.