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    • 1. 发明授权
    • Vapor phase process for preparing fluorinated aliphatic compounds
    • 制备含氟脂肪族化合物的气相法
    • US5981814A
    • 1999-11-09
    • US46023
    • 1998-03-23
    • C. Bradford BoyceRandolph K. Belter
    • C. Bradford BoyceRandolph K. Belter
    • C07C17/21C07C17/08
    • C07C17/21
    • A process is disclosed for the preparation of a fluorinated aliphatic hydrocarbon having the formulaCH.sub.a F.sub.3-a --CH.sub.2 --CH.sub.b F.sub.3-bwherein a is 0 or the integer 1 or 2 and b is 0 or the integer 1, 2 or 3. The reaction occurs in the vapor phase. A chlorofluoro olefin of the formulaCH.sub.c Cl.sub.2-c .dbd.CH--CH.sub.d F.sub.3--dwherein c is 0 or the integer 1 or 2, and d is 0 or the integer 1 or 2 is treated in the vapor phase with hydrogen fluoride. This treating is catalyzed with a compound that is a metal oxide, a metal halide or a mixture thereof. The metallic part of such compound is selected from a metal in Group IIIa, IIIb, IVa, Va, IVb, Vb, VIa, VIb, VIIb and VIII of the Periodic Table of the Elements. The treating is carried out for a time sufficient to form the desired fluorinated aliphatic hydrocarbon which is subsequently recovered from the vapor phase reaction.The process is particularly suitable for the preparation of 1,1,1,3,3-pentafluoropropane.
    • 公开了制备具有式CH 3 F a-CH 2 -CH b F 3-b的氟化脂族烃的方法,其中a为0或整数1或2,b为0或整数1,2或3.该反应发生在 汽相。 式C cCl 2 -C = CH-CH 3 F 3 -d c的氯氟烯烃为0或整数1或2,d为0或整数1或2在氟化氢气相中处理。 该处理用金属氧化物,金属卤化物或其混合物的化合物催化。 这种化合物的金属部分选自元素周期表的IIIa,IIIb,IVa,Va,IVb,Vb,VIa,VIb,VIIb和VIII族的金属。 进行处理足以形成所需的氟化脂族烃的时间,随后从汽相反应中回收。 该方法特别适用于制备1,1,1,3,3-五氟丙烷。
    • 2. 发明授权
    • Alumina based adsorbent containing alkali metal compounds
    • 基于氧化铝的吸附剂含有碱金属化合物
    • US5935894A
    • 1999-08-10
    • US886993
    • 1997-07-02
    • Vladislav I. Kanazirev
    • Vladislav I. Kanazirev
    • B01J20/08B01J23/02B01J23/04B01J20/04B01J21/04
    • B01J20/08B01J23/02B01J23/04
    • A method of preparing an alumina-based bodies suitable for use as an adsorbent or catalyst, the method comprising providing a source of activated alumina powder for forming into bodies and providing an aqueous solution containing at least two different alkali metals, at least one alkali metal derived from a soluble carboxylic acid alkali metal salt. As said powder is formed into said bodies, the bodies are contacted or sprayed with the aqueous solution to provide composite bodies containing the alumina powder and the alkali metals and the soluble carboxylic acid alkali metal salt. Alternatively, the alumina bodies may be formed first and then contacted, e.g., soaked in the aqueous solution. Or, a viscous slurry of the activated alumina powder and the aqueous solution may be made. The viscous slurry may be made into bodies by extrusion or by the oil drop method. Thereafter, the bodies are thermally treated to activate alumina therein and remove or decompose the organic part, e.g., carboxylic acid, of the soluble carboxylic acid alkali metal salt.
    • 一种制备适合用作吸附剂或催化剂的氧化铝基体的方法,所述方法包括提供用于形成体的活性氧化铝粉末源,并提供含有至少两种不同碱金属的水溶液,至少一种碱金属 衍生自可溶性羧酸碱金属盐。 当所述粉末形成所述体时,将体与水溶液接触或喷雾,以提供含有氧化铝粉末和碱金属和可溶性羧酸碱金属盐的复合体。 或者,可以首先形成氧化铝体,然后接触,例如浸泡在水溶液中。 或者,可以制备活性氧化铝粉末和水溶液的粘稠浆液。 粘稠浆料可以通过挤压或油滴法制成体内。 此后,将物体热处理以在其中活化氧化铝,并除去或分解可溶性羧酸碱金属盐的有机部分,例如羧酸。
    • 4. 发明授权
    • High temperature chlorination process for the preparation of
polychloroolefins
    • 用于制备聚氯烯的高温氯化工艺
    • US5689020A
    • 1997-11-18
    • US614005
    • 1996-03-11
    • C. Bradford Boyce
    • C. Bradford Boyce
    • C07C17/10C07C21/04
    • C07C21/04C07C17/10
    • A process is disclosed for preparing a compound selected from the group consisting of 1,1,3,3-tetrachloropropene and 1,3,3,3-tetrachloropropene. The process comprises a. admixing a hydrocarbon compound selected from the group consisting of propene, 1-chloropropene, 3-chloropropene, 1,1-dichloropropene, 1,3-dichloropropene, 3,3,-dichloropropene, 1,1-dichloropropane, 11,2-dichloropropane, 1,3-dichloropropane, 1,1,3-trichloropropene, 1,3,3-trichloropropene, 3,3,3-trichloropropene, and mixtures thereof with an inert diluent gas; b. preheating said mixture to from about 300.degree. C. to about 400.degree. C. and then mixing it with chlorine gas; and c. thermally treating the mixture of step b. at a temperature of from about 400.degree. C. to about 600.degree. C. The desired tetrachloropropene is then separated.
    • 公开了制备选自1,1,3,3-四氯丙烯和1,3,3,3-四氯丙烯的化合物的方法。 该方法包括a。 混合选自丙烯,1-氯丙烯,3-氯丙烯,1,1-二氯丙烯,1,3-二氯丙烯,3,3, - 二氯丙烯,1,1-二氯丙烷,11,2-二氯丙烷 ,1,3-二氯丙烷,1,1,3-三氯丙烯,1,3,3-三氯丙烯,3,3,3-三氯丙烯及其与惰性稀释气体的混合物; b。 将所述混合物预热至约300℃至约400℃,然后与氯气混合; 和c。 热处理步骤b的混合物。 在约400℃至约600℃的温度下,然后分离所需的四氯丙烯。
    • 6. 发明授权
    • Process for preparing fluorinated aliphatic compounds
    • 氟化脂肪族化合物的制备方法
    • US5616819A
    • 1997-04-01
    • US519779
    • 1995-08-28
    • C. Bradford BoyceRandolph K. Belter
    • C. Bradford BoyceRandolph K. Belter
    • C07C17/087C07C17/00C07C17/21C07C17/38C07C19/08C07C17/08
    • C07C17/38C07C17/206C07C17/21
    • A process is disclosed for the preparation of a fluorinated aliphatic olefin having the formulaCH.sub.a F.sub.3-a --CH.sub.2 --CH.sub.b F.sub.3-bwherein a is 0 or the integer 1 or 2 and b is 0 or the integer 1, 2 or 3.In the first step of the process, a chlorinated olefinic hydrocarbon of the formulaCH.sub.c Cl.sub.2-c .dbd.CH--CH.sub.d Cl.sub.3-dwherein c is 0 or the integer 1 and d is 0 or the integer 1 or 2 is reacted with anhydrous hydrogen fluoride for a period of time and at a temperature sufficient to form a chlorofluoro olefin of the formulaCH.sub.e Cl.sub.2-e .dbd.CH--CH.sub.f F.sub.3-fwherein e is 0 or the integer 1 and f is 0 or the integer 1 or 2.The chlorofluoro olefin produced in the first step is then reacted with anhydrous hydrogen fluoride in a second reaction. This second reaction is catalyzed with at least one compound that is a metal oxide or metal halide. Mixtures of said metal oxides, metal halides and metal oxides with metal halides may also be used. The metallic part of such compound is arsenic, antimony, tin, boron or is selected from a metal in Group IVb, Vb. VIb. VIIb or VIIIb of the Periodic Table of the Elements.The desired fluorinated aliphatic hydrocarbon is subsequently separated and recovered.The process is particularly suitable for the preparation of 1,1,1,3,3-pentafluoropropane.
    • 公开了制备具有式CH 3 F a-CH 2 -CH b F 3-b的氟化脂族烯烃的方法,其中a为0或整数1或2,b为0或整数1,2或3.在第一步中 该方法中,c为C = CH-CHCl 3-d的氯化烯烃,其中c为0或整数1,d为0或整数1或2与无水氟化氢反应一段时间,温度为 足以形成式CHeCl 2 -e = CH-CHFF 3 -F的氯氟烯烃,其中e为0或整数1,f为0或整数1或2.然后将第一步中产生的氯氟烯烃与无水氟化氢 在第二反应。 该第二反应用至少一种作为金属氧化物或金属卤化物的化合物催化。 也可以使用所述金属氧化物,金属卤化物和金属氧化物与金属卤化物的混合物。 这种化合物的金属部分是砷,锑,锡,硼或选自组IVb,Vb中的金属。 VIb。 元素周期表VIIb或VIIIb。 随后分离和回收所需的氟化脂族烃。 该方法特别适用于制备1,1,1,3,3-五氟丙烷。
    • 7. 发明授权
    • Process for the reducing emissions during prilling of material such as
ammonium nitrate
    • 在造粒诸如硝酸铵等材料时减少排放的过程
    • US5514307A
    • 1996-05-07
    • US280245
    • 1994-07-25
    • Arthur R. Shirley, Jr.Phillip A. ForsytheWilliam M. GilesJohn A. Phillips
    • Arthur R. Shirley, Jr.Phillip A. ForsytheWilliam M. GilesJohn A. Phillips
    • B01J2/04C05C1/02C05C9/00C05G3/00
    • C05G3/0058B01J2/04C05C1/02C05C9/005
    • This invention relates to an improvement in prilling whereby water is atomized into a prill tower to affect faster solidification of the prill, and in particular, the outside surface of the prill by providing an increased rate of surface cooling while reducing the required air flows in the tower. This results in a major reduction in air pollution potential in the form of both fume and particulate while at the same time allowing substantial production rate increases. Specifically, the invention relates to quick freezing the outside surface of the prill by flash evaporation of finely atomized water particles on the surface of the prill or in extremely close proximity to the prill to greatly lower the vapor pressure at the prill's surface and by continued flash evaporation to enhance cooling so as to allow upward flowing air to be reduced to a point where micro-prills which are formed in prilling can settle in the prill tower while obtaining the same or increased production rates. More specifically, the present invention relates to an improvement in melt prilling of water sensitive materials, in particular, ammonium nitrate, urea, potassium nitrate and other water soluble melts which normally absorb water or go into solution readily at ambient conditions in their solid state.
    • 本发明涉及造粒的改进,其中水被雾化成造粒塔,以通过提供增加的表面冷却速率来影响颗粒的更快凝固,特别是造粒的外表面,同时减少所需的空气流 塔。 这导致大气中的烟气和微粒形式的空气污染潜力的大幅减少,同时允许大量的生产率增加。 具体而言,本发明涉及通过在颗粒表面上微细雾化的水颗粒的闪蒸或者非常接近于颗粒的方式快速冷冻颗粒的外表面,以大大降低颗粒表面的蒸汽压力并持续闪光 蒸发以增强冷却,以允许向上流动的空气减少到在造粒中形成的微小颗粒可以在获得相同或增加的生产率的同时沉淀在造粒塔中。 更具体地说,本发明涉及水溶性材料,特别是硝酸铵,尿素,硝酸钾和其它水溶性熔体的熔融造粒的改进,其通常在固态环境条件下吸收水或溶解在溶液中。
    • 8. 发明授权
    • Process for separating and recovering hydrogen fluoride from mixtures
    • 从混合物中分离和回收氟化氢的方法
    • US5973215A
    • 1999-10-26
    • US39515
    • 1998-03-16
    • Randolph K. Belter
    • Randolph K. Belter
    • C01B7/19C07C17/38
    • C01B7/195C07C17/38
    • A process is disclosed for the liquid phase separation and recovery of hydrogen fluoride from a mixture comprising hydrogen fluoride and a fluorinated organic hydrocarbon. The process requires that the mixture be treated with a sufficient amount of a coupled phase-separating agent comprising an organic or inorganic salt, an alkanolamine or mixtures thereof and a substituted or unsubstituted aromatic compound to form a first and a second phase. The first phase that is formed is a hydrogen fluoride-rich phase that additionally contains substantially all of said salt, said alkanolamine or mixtures thereof from the coupled phase-separating agent. The second phase comprises substantially all of said aromatic compound and the fluorinated organic hydrocarbon. It is substantially free of hydrogen fluoride. The phases are separated from each other. Hydrogen fluoride and the salt, alkanolamine or mixtures thereof are then recovered from the separated first phase and the aromatic compound and fluorinated organic hydrocarbon are recovered from the separated second phase.
    • 公开了从包含氟化氢和氟化有机碳氢化合物的混合物中液相分离和回收氟化氢的方法。 该方法要求将混合物用足够量的包含有机或无机盐,链烷醇胺或其混合物和取代或未取代的芳族化合物的偶联相分离剂处理以形成第一和第二相。 所形成的第一相是富含氟化氢的相,其还含有基本上所有的所述盐,所述链烷醇胺或其来自偶联相分离剂的混合物。 第二相包括基本上所有的芳族化合物和氟化有机碳氢化合物。 它基本上不含氟化氢。 相分离。 然后从分离的第一相回收氟化氢和盐,链烷醇胺或其混合物,并从分离的第二相回收芳族化合物和氟化有机碳氢化合物。
    • 9. 发明授权
    • Vapor phase process for preparing fluorinated aliphatic compounds
    • 制备含氟脂肪族化合物的气相法
    • US5910616A
    • 1999-06-08
    • US100997
    • 1998-06-22
    • C. Bradford BoyceRandolph K. Belter
    • C. Bradford BoyceRandolph K. Belter
    • B01J27/12C07C17/21C07C17/08
    • B01J27/12C07C17/21
    • A process is disclosed for the preparation of a fluorinated aliphatic hydrocarbon. The process utilizes a C.sub.1 to C.sub.6 hydrocarbon substituted with a halogen selected from the group consisting of chlorine, bromine and iodine as the starting material. The alkyl hydrocarbon is reacted in the vapor phase at a temperature from about 75.degree. to about 150.degree. C. with hydrogen fluoride and a catalytically effective amount of at least one antimony compound having the formulaSb.sub.w.sup.u M.sub.x.sup.v X.sub.y F.sub.z.nHFwhere n is 0 or an integer that is at least 1; M is selected from the group consisting of a metal from Group IIIa, IIIb, IVa, IVb, Va, Vb, VIa, VIb, VIIb and VIII of the Periodic Table of the Elements; X is chloro, bromo or iodo; u is an integer that is the valence of antimony; v is an integer that is the valence of M; w, x and z are an integer of at least 1; y is 0 or an integer of at least 1; and (w.multidot.u)+(x.multidot.v)=y+z said at least one antimony compound being a nonvolatile solid at the temperature of the reaction, for a time sufficient to form said fluorinated aliphatic hydrocarbon.In order to conduct the process of the present invention, the antimony compound must be a nonvolatile solid at the temperature of the reaction. The reaction is carried out for a time sufficient to form said fluorinated aliphatic hydrocarbon.The fluorinated aliphatic hydrocarbon is subsequently separated from the vapor phase reactants and recovered.The process is particularly suitable for the preparation of 1,1,1,3,3-pentafluoropropane.
    • 公开了制备氟化脂族烃的方法。 该方法利用被选自氯,溴和碘的卤素取代的C1-C6烃作为起始原料。 烷基烃在气相中在约75℃至约150℃的温度下与氟化氢反应,并且催化有效量的至少一种具有式为SbwuMxvXyFz.nHF的锑化合物,其中n为0或位于 至少1; M选自元素周期表的IIIa,IIIb,IVa,IVb,Va,Vb,VIa,VIb,VIIb和VIII族的金属; X是氯,溴或碘; u是锑的化合价的整数; v是M的化合价的整数; w,x和z是至少为1的整数; y为0或至少为1的整数; 和(wxu)+(xxv)= y + z表示在反应温度下至少一种锑化合物为非挥发性固体,足以形成所述含氟脂族烃。 为了进行本发明的方法,锑化合物在反应温度下必须是非挥发性固体。 反应进行足以形成所述氟化脂族烃的时间。 随后将氟化脂族烃与气相反应物分离并回收。 该方法特别适用于制备1,1,1,3,3-五氟丙烷。