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    • 2. 发明公开
    • Verfahren und Vorrichtung zur Behandlung heisser Abgase, insbesondere von Gasturbinen
    • 用于治疗热废气,特别是燃气涡轮机的方法和装置。
    • EP0132452A1
    • 1985-02-13
    • EP83107444.8
    • 1983-07-28
    • Funk, Harald F., Dr.
    • Funk, Harald F., Dr.
    • F02C7/10
    • F02C7/10
    • Heiße Abgase, insbesondere von einer Gasturbine, werden in im Wechseltakt betriebenen Regeneratoren abgekühlt und mit der so gewonnen Wärme ein unter Druck gesetztes Arbeitsmedium aufgewärmt. Hierdurch wird die Abwärme, im Gegensatz zu üblichen Wärmetauschern auf einem höheren Enthalpieniveau wiedergewonnen, so daß das Arbeitsmedium zur Arbeitsleistung in einer Expansions-Kraftmaschine, z.b. einer Expansionsturbine, eingesetzt werden kann. Die Behandlung in den Regeneratoren zur Übertragung der Wärme auf das Arbeitsmedium kann in vorteilhafterweise mit einer weiteren Behandlung zum Entfernen von auf den Kühlflächen der Regeneratoren kondensierenden Verunreinigungen aus dem Abgas kombiniert werden.
    • 热的废气,特别是燃气涡轮机,被冷却以脉冲再生器,并且热被用来加热由此获得的一个加压的工作介质。 其结果是,与传统的热交换器,所述废热以高焓水平回收,所以没有工作介质可用于在膨胀马达来执行工作,对于膨胀涡轮的实施例。 用于发射的热量的工作介质在蓄热室的处理可以有利地与用于从所述废气中的杂质冷凝走上再生器的冷却表面上除去进一步的处理相结合。
    • 3. 发明公开
    • Solid waste refining and conversion to methanol
    • Raffinierung fester Abfallstoffe und Umwandlung在甲醇中。
    • EP0444684A2
    • 1991-09-04
    • EP91103045.0
    • 1991-02-28
    • Funk, Harald F., Dr.
    • Funk, Harald F., Dr.
    • C10J3/02C07C29/00C07C29/151
    • C10J3/02C07C29/1518C10J2300/0906C10J2300/1665C10J2300/1815C10K1/004C10K1/026C10K3/00C10K3/04Y02E50/32Y02P20/582C07C31/04
    • A process for converting solid waste into a synthesis suitable for producing liquid fuel, comprising (a) partially oxidizing and combusting solid waste material in a closed combustion zone at a temperature of 800-1000°C. and at a pressure below ambient to produce combustion gases by introducing into the combustion zone a gaseous oxidant comprising oxygen having a purity of at least 95% by volume and carbon dioxide in an oxygen to carbon dioxide ratio, by volume, of about 50:50, (b) conducting the combustion gases, oxygen and carbon dioxide through the solid waste material; (c) withdrawing a producer gas comprising the combustion gases and any unreacted oxygen and carbon dioxide; (d) removing particulate matter from the producer gas; (e) separating carbon dioxide from the producer gas and recycling a portion of the separated carbon dioxide to the combustion zone; (f) separating the less volatile, condensable components of the carbon dioxide-free producer gas, from the more volatile, non-condensable synthesis gas components thereof, and (g) compressing the producer gas at some time prior to the completion step (e). In a preferred embodiment, the more volatile components and at least a portion of the separated carbon dioxide from step (e) are admixed and the resulting admixed gas mixture is reacted to form methanol. Preferably, the less volatile components are converged by chemical reaction to hydrogen and the hydrogen is recycled into admixture with the producer gas at some time prior to the commencement of step (e).
    • 一种将固体废物转化成适合于生产液体燃料的合成物的方法,包括(a)在800-1000℃的温度和低于环境温度的封闭燃烧区中部分氧化和燃烧固体废料,以产生燃烧 气体通过将具有至少95体积%的纯度的氧气和氧二氧化碳比(体积比)为约50:50的二氧化碳引入燃烧区域,(b)导入燃烧气体, 氧气和二氧化碳通过固体废物; (c)取出包含燃烧气体和任何未反应的氧气和二氧化碳的生产气体; (d)从生产气体中除去颗粒物质; (e)从生产气体中分离二氧化碳,并将一部分分离的二氧化碳再循环到燃烧区; (f)将不含二氧化碳的生产气体的挥发性较低的可冷凝组分与较易挥发的不可冷凝的合成气组分分离,和(g)在完成步骤之前的某个时间压缩生产气体(e )。 在优选的实施方案中,混合来自步骤(e)的挥发性较高的组分和至少一部分分离的二氧化碳,并将所得的混合气体混合物反应形成甲醇。 优选地,较不易挥发的组分通过化学反应会聚到氢气中,并且氢气在步骤(e)开始之前的某个时间被再循环到与生产气体的混合物中。
    • 4. 发明公开
    • Solid waste refining and conversion to methanol
    • 固体废物精炼和甲醇转化
    • EP0444684A3
    • 1991-11-21
    • EP91103045.0
    • 1991-02-28
    • Funk, Harald F., Dr.
    • Funk, Harald F., Dr.
    • C10J3/02C07C29/00C07C29/151
    • C10J3/02C07C29/1518C10J2300/0906C10J2300/1665C10J2300/1815C10K1/004C10K1/026C10K3/00C10K3/04Y02E50/32Y02P20/582C07C31/04
    • A process for converting solid waste into a synthesis suitable for producing liquid fuel, comprising (a) partially oxidizing and combusting solid waste material in a closed combustion zone at a temperature of 800-1000°C. and at a pressure below ambient to produce combustion gases by introducing into the combustion zone a gaseous oxidant comprising oxygen having a purity of at least 95% by volume and carbon dioxide in an oxygen to carbon dioxide ratio, by volume, of about 50:50, (b) conducting the combustion gases, oxygen and carbon dioxide through the solid waste material; (c) withdrawing a producer gas comprising the combustion gases and any unreacted oxygen and carbon dioxide; (d) removing particulate matter from the producer gas; (e) separating carbon dioxide from the producer gas and recycling a portion of the separated carbon dioxide to the combustion zone; (f) separating the less volatile, condensable components of the carbon dioxide-free producer gas, from the more volatile, non-condensable synthesis gas components thereof, and (g) compressing the producer gas at some time prior to the completion step (e). In a preferred embodiment, the more volatile components and at least a portion of the separated carbon dioxide from step (e) are admixed and the resulting admixed gas mixture is reacted to form methanol. Preferably, the less volatile components are converged by chemical reaction to hydrogen and the hydrogen is recycled into admixture with the producer gas at some time prior to the commencement of step (e).
    • 5. 发明公开
    • System for solar energy collection and recovery
    • 系统zur Sammlung und Wiedergewinnung von Sonnenenergie。
    • EP0229373A1
    • 1987-07-22
    • EP86117896.0
    • 1986-12-22
    • Funk, Harald F., Dr.
    • Funk, Harald F., Dr.
    • F02C1/05F02C6/14F24J2/10
    • B01D53/005C10J3/06F02C1/05F02C6/14F02C6/18F23J15/006F23J15/06F23J2215/10F23J2215/20F23J2215/30F23J2215/40F23J2215/50F23J2217/10F23J2217/40F23J2219/70F24S20/20F24S2020/23F28D2021/0019Y02E10/41Y02E20/363Y02P20/129Y02P20/134
    • A system for the collection of solar radiation and the recovery of thermal energy therefrom includes solar radiation receiver means (18) at or near the focus (24) of a solar radiation concentrating means (16) for absorbing the solar radiation, converting it to thermal energy and transferring the thermal energy to ambient air drawn over the receiver means (18) and, thereafter, directed to an energy reclamation unit (200). In the energy reclamation unit (200) the heated ambient air deposits a portion of its thermal energy in regenerators (50, 52), from which it is recovered by a compressed air stream, and transfers a portion of its thermal energy to a power fluid. The thermal energy of the ambient air is reclaimed from the compressed air stream and the power fluid as shaft work in expansion turbines (72,88). In a preferred embodiment, the solar radiation receiver (18) means comprises a high temperature resistant, porous, convex enclosure having inner (45) and outer (44) porous, convex surfaces arranged in spaced apart nested relationship for defining therebetween an annular space (46) which is randomly filled with a plurality of close to ideal black body solar radiation absorbing elements (47).
    • 用于收集太阳辐射和从其中回收热能的系统包括太阳辐射接收装置(18),太阳辐射接收装置(18)在用于吸收太阳辐射的太阳辐射集中装置(16)的焦点(24)附近或附近,将其转换成热 能量并将热能转移到在接收装置(18)上抽取的环境空气,之后被引导到能量回收单元(200)。 在能量回收单元(200)中,加热的环境空气将其热能的一部分沉积在再生器(50,52)中,通过压缩空气流将其回收,并将其热能的一部分转移到动力流体 。 环境空气的热能从压缩空气流中回收,动力流体作为轴在膨胀涡轮机中工作(72,88)。 在优选实施例中,太阳辐射接收器(18)包括耐高温,多孔的凸形外壳,其具有以间隔开的嵌套关系布置的内(45)和外(44)多孔凸表面,用于在其间限定环形空间 46),其随机填充有多个接近理想的黑体太阳辐射吸收元件(47)。