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    • 2. 发明授权
    • Method for hydrotreating and upgrading heavy crude oil during production
    • 生产过程中重质原油的加氢处理和升级方法
    • US5824214A
    • 1998-10-20
    • US504052
    • 1995-07-11
    • James M. PaulR. Michael Davis
    • James M. PaulR. Michael Davis
    • C10G15/08C10G45/24C10G45/26E21B43/00E21B43/16C01G47/00C09K7/00C01B53/00
    • C10G15/08C10G45/24C10G45/26E21B43/003E21B43/162
    • Heavy crude oil containing at least 1% by weight water is hydrotreated and upgraded while being produced downhole in a production well. During production the heavy crude oil containing water is subjected to sonic energy at a low frequency of 400 Hz to 10 kHz downhole in the presence of a metal hydrogenation catalyst that causes the water in the crude oil to react and form hydrogen which then hydrotreats and upgrades the heavy crude oil during production. In another embodiment, if the heavy crude oil does not contain water, the hydrogen may be formed in-situ by contacting the heavy crude oil downhole with a chemical compound comprising ammonia, hydrazine and formic acid that in the presence of a metal hydrogenation catalyst and sonic energy causes the chemical compound to react and form hydrogen which then hydrotreats the heavy crude oil during production. Suitable catalysts include nickel on zinc dust, platinum on carbon and palladium on carbon, preferably nickel on zinc dust. The hydrotreated and upgraded heavy crude oil has improved properties making it easier to refine and transport by pipeline. The upgrading includes reducing the amount of asphaltenes and resins in the heavy crude oil and increasing the amount of aromatics and saturates.
    • 含有至少1重量%水的重质原油在生产井中生产井下时进行加氢处理和升级。 在生产过程中,在金属加氢催化剂存在下,含水的重质原油在400Hz至10kHz的低频率下经受声能,其导致原油中的水反应并形成氢气,然后进行加氢处理和升级 生产中的重质原油。 在另一个实施方案中,如果重质原油不含水,则可以通过使井下的重质原油与包含氨,肼和甲酸的化合物接触来原位形成氢,所述化合物在金属氢化催化剂存在下和 声能导致化合物反应并形成氢气,然后在生产过程中对重质原油进行加氢处理。 合适的催化剂包括锌粉上的镍,碳上的铂和碳上的钯,优选在锌粉上的镍。 加氢处理和升级的重质原油具有改进的性质,使其更容易通过管道精炼和运输。 升级包括减少重质原油中沥青质和树脂的数量,增加芳烃和饱和物的用量。
    • 3. 发明授权
    • Method for scale removal in a wellbore
    • 在井筒中除垢的方法
    • US5183112A
    • 1993-02-02
    • US745779
    • 1991-08-16
    • James M. PaulRichard L. Morris
    • James M. PaulRichard L. Morris
    • C09K8/528E21B37/06
    • E21B37/06C09K8/528
    • Alkaline earth metal scales, especially barium sulfate scale is removed from a well (the wellbore and the adjacent formation) by contacting the scale with a scale-removing solvent and thereafter sparging the solvent with air or insert gas to dissolve the scale. The sparging aids in achieving a flushing action by the solvent relative to the scale thereby enabling the solvent to more effectively dissolve the scale in the well. Temperature and caustic compatible surfactuants (anionic and non-ionic) may be used in the solvent to generate a column of foam which increases the extent of cleaning oil from the scale surfaces, enabling the solvent to more effectively remove the scale.
    • 通过使水垢与除垢溶剂接触,然后用空气或插入气体喷射溶剂以溶解氧化皮,从井(井筒和相邻地层)中除去碱土金属垢,特别是硫酸钡垢。 喷射有助于通过溶剂实现相对于氧化皮的冲洗作用,从而使溶剂能够更有效地溶解阱中的氧化皮。 可以在溶剂中使用温度和苛性相容的表面活性剂(阴离子和非离子)以产生泡沫柱,其增加了从刻度表面清洗油的程度,使得溶剂能够更有效地除去垢。
    • 4. 发明授权
    • Method for regenerating scale solvent
    • 再生规模溶剂的方法
    • US5151196A
    • 1992-09-29
    • US766313
    • 1991-09-27
    • James M. PaulRichard L. Morris
    • James M. PaulRichard L. Morris
    • C02F5/12C09K8/528C23G1/36
    • C23G1/36C02F5/12C09K8/528
    • Barium sulfate scale is dissolved by contacting the scale with an aqueous solvent having a pH of about 10 to about 14, preferably about 12, and comprising a chelating agent comprising a polyaminopolycarboxylic acid or salt of such an acid, and a synergist anion. The solvent containing the dissolved scale is regenerated by acidifying the spent solvent with an acidic chelating agent such as EDTA or DTPA, preferably DTPA, that release alkaline earth cations which react with sulfate ions present in the solvent to form a precipitate of an insoluble salt of the alkaline earth metal. The precipitate is then removed from the solvent by settling/decanting, filtering, or centrifuging. Thereafter, caustic is added to increase the pH of the solvent to a pH of about 10 to about 14, preferably about 12, to recover a regenerated solvent for reuse, in dissolving scale. The amount of chelating agent added to acidify the spent solvent balances the total amount of dilution caused by adding the caustic thereby maintaining the activity of the chelating agent in the regenerated solvent at least equivalent to or greater than the activity in the spent solvent.
    • 通过使水垢与约10至约14,优选约12的pH的水性溶剂接触并包含包含聚氨基多羧酸或这种酸的盐的螯合剂和增效剂阴离子来使溶解硫酸钡垢。 含有溶解垢的溶剂通过用酸性螯合剂如EDTA或DTPA(优选DTPA)酸化废溶剂来再生,其释放与存在于溶剂中的硫酸根离子反应的碱土金属阳离子,以形成不溶性盐的沉淀物 碱土金属。 然后通过沉降/倾析,过滤或离心从溶剂中除去沉淀物。 此后,加入苛性碱以将溶剂的pH增加至约10至约14,优选约12的pH,以回收再生溶剂以在溶解氧化垢中再次使用。 用于酸化废溶剂的螯合剂的量平衡通过加入苛性碱引起的稀释总量,从而保持再生溶剂中螯合剂的活性至少等于或大于废溶剂中的活性。
    • 7. 发明授权
    • Method of stabilizing solutions of chelated polyvalent metals
    • 稳定螯合多价金属溶液的方法
    • US4784838A
    • 1988-11-15
    • US188054
    • 1988-04-26
    • James M. PaulEarl S. Snavely, Jr.
    • James M. PaulEarl S. Snavely, Jr.
    • B01D53/52C01B17/05C01B17/04
    • B01D53/52C01B17/05
    • A cyclic process for removing H.sub.2 S from a gaseous stream comprising contacting the gaseous stream with a solution of a chelated polyvalent metal to produce elemental sulfur, removing the elemental sulfur, and regenerating the reaction solution, e.g., by contacting it with oxygen, and recycling the regenerated solution to the reaction zone, is modified by introducing into the solution a free chelating agent. The introduction of the free chelating agent eliminates the loss of the polyvalent metal and the chelated polyvalent metal from the reaction solution.There is also disclosed an aqueous reaction solution comprising a chelated polyvalent metal, sulfur, and a free chelating agent in the amount equal to at least about 0.1% by weight of the amount of the chelated polyvalent metal in the solution.
    • 一种用于从气流中除去H 2 S的循环方法,包括使气态物流与螯合多价金属的溶液接触以产生元素硫,除去元素硫并再生反应溶液,例如通过使其与氧接触,并将 通过向游离溶液中引入游离螯合剂来修饰反应区的再生溶液。 引入游离螯合剂可以消除反应溶液中多价金属和螯合多价金属的损失。 还公开了包含螯合多价金属,硫和游离螯合剂的水溶液反应溶液,其量等于溶液中螯合多价金属的量的至少约0.1重量%。
    • 9. 发明授权
    • Use of variable density carrier fluids to improve the efficiency of
scale dissolution
    • 使用可变密度载体流体来提高垢溶解的效率
    • US5366016A
    • 1994-11-22
    • US164861
    • 1993-12-10
    • Eleanor R. FielerAlfred R. Jennings, Jr.James M. Paul
    • Eleanor R. FielerAlfred R. Jennings, Jr.James M. Paul
    • E21B37/00C09K8/528E21B37/06E21B43/28
    • E21B37/06C09K8/528
    • A method to improve the efficiency of scale dissolution in a formation containing multiple productive intervals where variable density liquids are utilized. Initially, a liquid composition sufficient to solubilize an alkaline-earth metal sulfate scale deposit is directed into a wellbore thereby contacting scale in one productive interval of the formation. Thereafter, a second scale solubilizing liquid having a density of about 0.1 wt % less than the first liquid is directed into the wellbore thereby contacting additional perforations and a higher interval. These scale solubilizing liquids with varying densities are allowed to remain in contact with perforations and productive intervals communicating therewith for a time sufficient to solubilize the scale deposit thereby efficiently removing said scale deposit from perforations and productive intervals at two different levels.
    • 一种提高含有可变密度液体的多个生产间隔的地层中的水垢溶解效率的方法。 最初,将足以溶解碱土金属硫酸盐垢沉积物的液体组合物导入井筒,从而在地层的一个生产间隔中接触氧化皮。 此后,具有比第一液体小约0.1重量%的密度的第二比例增溶液被引导到井眼中,从而接触另外的穿孔和更高的间隔。 允许具有不同密度的这些规模增溶液体与穿孔和与其连通的生产间隔保持接触足以溶解垢垢的时间,从而有效地从两个不同水平的穿孔和生产间隔去除鳞屑沉积物。