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    • 9. 发明申请
    • ISOMERIZATION PROCESS
    • 异构化过程
    • WO0132590A3
    • 2002-01-03
    • PCT/US0041437
    • 2000-10-23
    • BP CORP NORTH AMERICA INC
    • TWU FRED CHUN-CHIENCOX WILLIAM L
    • C09K8/36C07B61/00C07C5/25C07C5/27C07C11/02C09K8/04C09K8/34C09K7/06
    • C09K8/34C07C5/2512C07C5/2772C07C11/02
    • A method for isomerizing a linear alpha olefin mixture comprising vinyl and vinylidine olefins containing from 10 to 35 carbon atoms, comprising: contacting the alpha olefin mixture in the gas or liquid phase with a bed of porous solid acid ctalyst particles comprising gamma lumina having a specific surface area of at least 100 square meters per gram, a pore volume of at least 0.4 cubic centimeter per gram, an average pore diameter of at least 30 Angstroms, a sodium content of less than 0.01 weight percent and an ammonia chemissorption of at least 0.1 millimole per gram, at a reaction temperature in the range of from about 200 DEG C to about 400 DEG C, a reaction pressure in the range of from about 15 to about 500 pounds per square inch absolute and a weight hourly space velocity of from about 0.5 to about 20 kilograms of olefin mixture per kilogram of catalyst particles per hour, wherein the reaction temperature, pressure and weight hourly space velocity are selected so as to form a product mixture comprising at least 70 wight percent of di- and tri-substitued internal olefins, at least 20 weight percent of which product mixture are di-substituted internal olefins having a double bond at the fourth or higher numbered carbon atom position and less than 50 weight percent of which are di-substituted internal olefins having a double bond at the second or third numbered carbon atom position, and which has a kinematic viscosity less than 4 cSt measured at 40 DEG C. and a pour point below -25 DEG C.
    • 一种使包含含10至35个碳原子的乙烯基和亚乙烯基烯烃的线性α-烯烃混合物异构化的方法,包括:将气相或液相中的α-烯烃混合物与包含具有特定的 表面积至少为100平方米/克,孔体积至少为0.4立方厘米每克,平均孔径至少为30埃,钠含量小于0.01重量%,氨化学吸附为至少0.1 在约200℃至约400℃的反应温度下,反应压力范围为约15至约500磅/平方英寸绝对值,重时空速为约 每小时每千克催化剂颗粒0.5至约20千克烯烃混合物,其中选择反应温度,压力和重量时空速度以形成p 包含至少70%的二和三取代的内烯烃的至少20重量%的产物混合物,其中该产物混合物是在第四个或更高编号的碳原子位置具有双键的二取代的内烯烃,小于50 其重量百分比是在第二或第三编号的碳原子位置具有双键的二取代的内烯烃,并且其在40℃下测得的运动粘度小于4cSt,倾点低于-25℃。
    • 10. 发明申请
    • METHOD FOR USING BIODEGRADABLE DRILLING FLUID
    • 使用可生物降解钻井液的方法
    • WO00005324A1
    • 2000-02-03
    • PCT/FR1999/001773
    • 1999-07-20
    • C09K8/34C09K8/36C09K7/06
    • C09K8/34C09K8/36
    • The invention concerns a method for using biodegradable fluid characterised in that it consists, at the very start of drilling, in introducing into the well a biodegradable surface sludge stable up to about 100 DEG C, with filtrate reducing power adjustable from 2 to 13 cm depending on the amount of filtrate reducing agent used, and with electric stability not less than 1000 volts, and when the temperature of the terrain being traversed reaches 100 DEG C, in replacing said surface sludge by a bottom sludge stable at a temperature higher than 200 DEG C, the surface sludge volume representing 60 to 80 % by volume of the total sludge used.
    • 本发明涉及一种使用可生物降解的流体的方法,其特征在于它在钻井开始时在井内引入高达约100℃稳定的可生物降解的表面污泥,其中滤液还原能力可从2至13厘米 3>取决于所使用的滤液还原剂的量,电稳定性不低于1000伏,当穿越地形的温度达到100℃时,在较高温度下用底部污泥替代底部污泥 超过200℃,表面污泥体积占总污泥量的60〜80%。