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    • 5. 发明授权
    • Pulse combustion energy system
    • 脉冲燃烧能量系统
    • US4941820A
    • 1990-07-17
    • US261652
    • 1988-10-24
    • Hanford N. Lockwood, Jr.
    • Hanford N. Lockwood, Jr.
    • F02G1/02F23C1/08F23C15/00F26B17/10F26B23/02
    • F23C15/00F02G1/02F23C1/08F26B17/10F26B23/026F02G2254/11F02G2258/10
    • A pulse combustion energy system including a pulse combustor coupled to a processing tube for flowing material to be processed therethrough, the processing tube being coupled to a pair of cyclone collectors for receiving the material flowing therefrom. An optional recycling section is coupled to the cyclone collectors for flowing vapor from the cyclone collectors back to the upstream end of the processing tube. The pulse combustor includes a rotary valve, a combustion chamber, an inner tail pipe and an outer tail pipe. The combustion chamber and inner tail pipe are conical and tubular sections mounted in longitudinal compression, and the compressive forces are transmitted externally across the junction of the combustion chamber and tail pipe by a strongback assembly. The rotary valve includes first, second, and third closely adjacent cylinders defining an interior air chamber. The cylinders have radially oriented, substantially aligned apertures which define an air intake. Air passing from the air chamber into the combustion chamber passes through an annular passage which impedes air flow from the combustion chamber toward the air chamber to a greater extent than air flow from the air chamber to the combustion chamber. Control systems regulate the product feed rate, the system firing rate, the system flow rate, and the operating frequency of the pulse combustor.
    • 一种脉冲燃烧能量系统,包括连接到处理管的脉冲燃烧器,用于使要加工的材料流过其中,处理管与一对旋风收集器连接,用于接收从其流出的材料。 可选的回收部分连接到旋风分离器收集器,用于将蒸气从旋风分离器收集器回流到处理管的上游端。 脉冲燃烧器包括旋转阀,燃烧室,内尾管和外尾管。 燃烧室和内尾管是以纵向压缩方式安装的圆锥形和管状部分,并且压缩力通过强反射组件在燃烧室和尾管的接合处向外传输。 旋转阀包括限定内部空气室的第一,第二和第三紧密相邻的气缸。 气缸具有径向取向的,基本上对齐的孔,其限定进气口。 从空气室进入燃烧室的空气通过环形通道,该环形通道阻止从燃烧室朝向空气室的气流大于从空气室到燃烧室的气流。 控制系统调节产品进料速率,系统燃烧速率,系统流量和脉冲燃烧器的工作频率。
    • 6. 发明授权
    • Vapor stirling heat machine
    • 蒸汽斯特林热机
    • US4794752A
    • 1989-01-03
    • US49698
    • 1987-05-14
    • Roy H. Redderson
    • Roy H. Redderson
    • F02G1/044F02G1/05F25B9/14F03C5/00
    • F25B9/14F02G1/044F02G1/05F02G2244/00F02G2244/08F02G2254/30F02G2258/10F25B2309/1401
    • A heat machine which employs a condensing working fluid in a Stirling type mechanical arrangement. An initial mass of working fluid is contained within a closed space. Portions of hot and cold volumes are cyclically varied, which transfers a small percentage of the working fluid through large hot and cold heat exchangers interconnected with a periodic flow regenerator. With the exception of the regenerator space, the transferred working fluid is substantially in the liquid phase during the near isothermal heat rejection and compression stages, and substantially in the superheated vapor phase during the near isothermal heat addition and expansion stages. A control cylinder varies the effective mass of working fluid within the machine, so as to provide for output control. Decreasing the effective mass causes a shift in the operating cycle toward the superheated vapor region with lower mean pressure cycles, and increasing the mass causes a shift to the liquid region with higher mean pressure cycles. The large near isothermal heat exchangers assist in effective regeneration of the working fluid through the vapor dome, and further, provide considerable improvement in cycle thermal efficiencies. Also, the condensed working fluid requires less input work and the total cycle pressure/volume characteristics exhibit greater output work, especially during the expansion phase, than do conventional Stirling machines.
    • 采用斯特林式机械装置的冷凝工作流体的加热机。 工作流体的初始质量包含在封闭空间内。 热和冷量的部分是周期性变化的,其通过与周期性流量再生器互连的大型热和冷热交换器传送一小部分工作流体。 除了再生器空间之外,在接近等温热排斥和压缩阶段期间,转移的工作流体基本处于液相,并且在近等温热加入和膨胀阶段期间基本上处于过热气相中。 控制缸改变机器内工作流体的有效质量,从而提供输出控制。 降低有效质量导致操作循环向平均压力循环较低的过热蒸汽区域移动,并且增加质量导致以更高的平均压力循环向液体区域移动。 大的近等温热交换器有助于工作流体通过蒸汽圆顶的有效再生,并且进一步提供循环热效率的显着改进。 此外,冷凝的工作流体需要更少的输入功率,并且总循环压力/体积特性表现出比常规斯特林机器更大的输出功率,特别是在膨胀阶段。