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    • 1. 发明授权
    • Removal of sulfur dioxide from waste gases
    • 从废气中去除二氧化硫
    • US4208387A
    • 1980-06-17
    • US716160
    • 1976-08-20
    • Donald L. KlassJohn R. Conrad
    • Donald L. KlassJohn R. Conrad
    • B01D53/50C10K1/14C10K1/16C01B17/00
    • C10K1/143B01D53/507C10K1/16
    • Sulfur dioxide is removed from waste gases such as stack gases by contacting the gas stream with free tertiary amines having basic strengths greater than about pK 5 to form a coordinate covalent complex of the amine and the sulfur dioxide. The sufficiently stable complex is than thermally regenerated to liberate the sulfur dioxide in one stream, to provide the residual gases in another stream, and to provide the regenerated tertiary amine for collection and reuse in a subsequent sulfur dioxide cleanup step. The coordinate covalent complex reacts with even very small concentrations of sulfur dioxide to effectively reduce the sulfur dioxide to detectable zero levels. The presence of carbon dioxide in waste gas streams does not interfere with the efficient cleanup because the selected tertiary amine does not react with the carbon dioxide.
    • 通过将气流与具有大于约pK 5的碱性强度的游离叔胺接触以形成胺和二氧化硫的配位共价络合物,将二氧化硫从诸如烟道气体的废气中除去。 足够稳定的络合物不是热再生以在一个流中释放二氧化硫,以在另一个流中提供残余气体,并且提供再生的叔胺用于在随后的二氧化硫净化步骤中收集和再利用。 配位共价络合物与甚至非常小的二氧化硫浓度反应,以有效地将二氧化硫还原成可检测的零水平。 废气流中二氧化碳的存在不会干扰有效的净化,因为所选择的叔胺不与二氧化碳反应。
    • 6. 发明授权
    • Two phase anaerobic digestion
    • 两相厌氧消化
    • US4022665A
    • 1977-05-10
    • US530760
    • 1974-12-09
    • Sambhunath GhoshDonald L. Klass
    • Sambhunath GhoshDonald L. Klass
    • C02F3/28C02F3/34C12P5/02C12D3/10
    • C02F3/286C02F3/34C12P5/023Y02E50/343Y10S435/801Y10S435/819Y10S435/822
    • An improved two phase anaerobic digestion process in which an initial phase continually receives an organic feed for short detention times of less than two days under conditions which efficiently liquefy and breakdown the feed to lower molecular weight acids and other intermediates for conversion to methane. A succeeding phase is operated to treat the lower molecular weight acids and intermediates for detention times of about two to about seven days under conditions which efficiently lead to production of methane. The feed is loaded in the first phase at rates from about 1 to about 10 pounds of total organics per cubic foot per day; and the products from the initial phase are loaded in the succeeding phase at rates of about 0.1 to about 0.5 pounds total organics per cubic foot per day.
    • 一种改进的两相厌氧消化过程,其中初始阶段在有效地将进料液化并分解成低分子量酸和其它中间体以转化为甲烷的条件下,连续接收少于两天的短停留时间的有机进料。 在有效地导致甲烷生成的条件下,操作后续阶段来处理低分子量酸和中间体的滞留时间约2至约7天。 饲料在第一阶段以每立方英尺每天约1至约10磅总有机物的速率装载; 并且来自初始阶段的产物以相对于每立方英尺每天约0.1至约0.5磅总有机物的速率装载在后续阶段。
    • 8. 发明授权
    • Situ mining of fossil fuel containing inorganic matrices
    • 含有无机基质的化石燃料的原位采矿
    • US4085972A
    • 1978-04-25
    • US800357
    • 1977-05-25
    • Sambhunath GhoshDonald L. Klass
    • Sambhunath GhoshDonald L. Klass
    • C09K8/58C12M1/107E21B43/22C12B1/00E21C41/10
    • C09K8/58E21B43/16E21C41/24
    • A process for recovering underground fossil fuel deposits retained in an inorganic matrix wherein the deposit is contacted with an aqueous medium of anaerobic microorganisms for a time sufficient to produce particles of the deposit containing both the organic fossil fuel and inorganic matrix of a size capable of forming a slurry with the aqueous medium for pumping to the ground surface. At the ground surface, the particulates are separated from the aqueous medium of anaerobic organisms, the particulates further processed by efficient surface techniques to separate the organic carbon and hydrocarbon component from the inorganic matrix. The aqueous medium of anaerobic organisms is recycled to the underground fossil fuel deposit for further production of the slurry forming particles of the deposit. Spent inorganic matrix may be added to the aqueous medium of anaerobic organisms to provide solid support and nutrient for the organisms and to maintain the desired pH. Such use of the spent inorganic matrix provides a useful service for the waste from the organic carbon and hydrocarbon recovery process.
    • 一种回收保存在无机基体中的地下化石燃料沉积物的方法,其中沉积物与厌氧微生物的水性介质接触一段时间,足以产生含有能够形成的大小的有机化石燃料和无机基质的沉积物的沉积物 具有用于泵送到地面的水性介质的浆料。 在地表表面,颗粒与厌氧生物体的水性介质分离,颗粒通过有效的表面技术进一步处理,以将有机碳和烃组分与无机基质分离。 将厌氧生物的水性介质再循环到地下化石燃料沉积物中,以进一步生产沉积物形成的浆料颗粒。 可以将无机基质添加到厌氧生物体的水性介质中以为生物提供固体支持物和营养物并保持所需的pH。 废弃无机基质的这种使用为有机碳和烃回收过程中的废物提供了有用的服务。
    • 10. 发明授权
    • Two phase anaerobic digester system
    • 两相厌氧消化器系统
    • US4318993A
    • 1982-03-09
    • US793519
    • 1977-05-04
    • Sambhunath GhoshDonald L. Klass
    • Sambhunath GhoshDonald L. Klass
    • C02F3/28C02F3/34C12P5/02
    • C12M29/02C02F3/286C02F3/34C12M21/04C12M23/58C12M45/06C12P5/023Y02E50/343
    • A two phase anaerobic digestion process in which an initial phase continually receives an organic feed for short detention times of less than two days under conditions which efficiently liquefy and breakdown the feed to lower molecular weight acids and other intermediates for conversion to methane. A succeeding phase is operated to treat the lower molecular weight acids and intermediates for detention times of about two to about seven days under conditions which efficiently lead to production to methane. The feed is loaded in the first phase at rates from about one to about ten pounds of total organics per cubic foot per day; and the products from the initial phase are loaded in the succeeding phase at rates of about 0.1 to about 0.5 pounds total organics per cubic foot per day.
    • 在两相厌氧消化过程中,初始阶段在有效地将进料液化并分解成较低分子量的酸和其它中间体以转化为甲烷的条件下,连续接收少于两天的短停留时间的有机进料。 在有效地导致甲烷生产的条件下,运行后续阶段来处理较低分子量酸和中间体的滞留时间约2至约7天。 饲料在第一阶段以每立方英尺每天约1至约10磅总有机物的速率装载; 并且来自初始阶段的产物以相对于每立方英尺每天约0.1至约0.5磅总有机物的速率装载在后续阶段。