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123results about How to "Even flow distribution" patented technology

Adjustable air foils for balancing pulverized coal flow at a coal pipe splitter junction

InactiveUS20050042043A1Coal flow imbalanceIncreasing and decreasing flowFuel feeding arrangementsDamper arrangementPollutant emissionsCoal
An adjustable device installed at the inlet of conventional junctions/splitters (116) for on-line control of the distribution of coal among the outlet pipes is herein disclosed. The device includes a plurality of wake inducing airfoils (60) each positioned upstream of a plurality of flow channels in the riffler (50) for directing coal flow to the outlet pipes. Each wake-inducing airfoil has a cross-section defined by a width W that varies along its length H for creating upstream turbulence, and a particle wake that preferentially diverts the coal flow to one of the outlet pipes at the splitter junction without affecting primary air flow. For example, each wake inducing airfoil may comprise a rounded convex edge leading to straight tapered sides. The surfaces of the sides may be roughened or textured (63) for promoting turbulent boundary layers. In addition, conventional fixed or variable orifices may be used in combination with the wake inducing airfoils for balancing primary air flow rates. The device allows fine-adjustment control of coal flow rates when used in combination with the slotted riffler, yet it has negligible effect on the distribution of primary air, resulting in closely balanced coal flow, reduced pollutant emissions and improved combustion efficiency.
Owner:LEVY EDWARD KENNETH +3

Stepped downcomer apparatus and vapor-liquid contact apparatus with same

A stepped downcomer apparatus for use in a vapor-liquid contact apparatus having an intermediate level step platform with a preferred tri-edge peripheral edge and corresponding step panels extending down from that edge to form a sealing step panel wall. As a preferred support device, extensions extend in chordal fashion out from the interior vertical edge of the opposite side step wall panels and either directly or indirectly by way of support bars into a supporting relationship with a tower of the vapor-liquid contact apparatus. A main panel extends up from the interior edge of the platform and up to the above positioned tray. A weir may extend above the above positioned tray that is an extension of the main panel. This main panel is attached to the support bars and supports the step platform and walls and extensions either alone or with added support members. A tray support ledge extends inwardly from the downcomer to provide support to the upper tray. The liquid-vapor mix contacts the step platform after passing over the weir, and off from which fluid travels both along the central axis of flow and obliquely off the opposite side panels. At opposite ends of the weir, the liquid flows directly into contact with the inlet region of the lower tray, by-passing the platform. The opposite side panel walls can slope outward to vary the downcomer lower pass through volume. An embodiment features chordal wing extensions with pressure equalization openings that extends out from opposite sides of the step wall panel also into a support relationship with the tower. The lower edge of the panels of the wall and the lower edge of the extensions control the flow of fluid as it travels under the lower edging from the inlet side of the downcomer apparatus to the active area of the tray. The relative level of the lower edges can be varied to suit the intended use. Additional or replacement downcomer structural supports include vertical support members extending from a step panel to a lower tray either in the form of support brackets or tiplet extensions.
Owner:SULZER MANAGEMENT AG

Connection between cyclone separators and hearth of large-scale circulating fluidized bed boiler

The invention discloses connection between cyclone separators and a hearth of a large-scale circulating fluidized bed boiler. The hearth is connected with six cyclone separators. A cross section of the hearth is rectangular, wherein upper portions of two wider side walls of the hearth are provided with three flue gas outlets respectively. The six cyclone separators are divided into two sets equally and are fixedly connected with the two wider side walls. Each flue gas outlet is communicated with an inlet flue of the cyclone separator. Cylindrical shell structure and dimension of the six cyclone separator are same. In the two set of cyclone separators on the two side walls, inlet flue cross section of each cyclone separator of each set and inlet flue cross section of each cyclone separator of the other set form central symmetry relative to a central point of the hearth. Inlet flue cross sections of two outboard cyclone separators of the sets form axial symmetry relative to a center line of the hearth. According to the connection provided in the invention, flow of flue gas in the hearth is distributed uniformly, flue gas flux of each cyclone separator is distributed uniformly, particle concentration of a vertical cross section of the inlet flue is in reasonable distribution, thus performance consistency of each cyclone separator is ensured.
Owner:INST OF ENGINEERING THERMOPHYSICS - CHINESE ACAD OF SCI

Large-diameter laser liquid cooling mirror structure

InactiveCN104852257AUniform distribution of pressure and flowEven heat dissipationMountingsLaser cooling arrangementsBackplaneEngineering
The invention discloses a large-diameter laser liquid cooling mirror structure, which comprises a reflection panel, a distribution plate and a back plate, wherein the back face of the distribution plate is provided with water inlet first-level flow channels and water outlet first-level flow channels; the front face of the distribution plate is provided with water inlet second-level flow channels and water outlet second-level flow channels distributed parallelly; a plurality of water inlet holes and water outlet holes are arranged in the back plate; and the front face of the reflection panel is a reflection face, and the back face is provided with third-level flow channels. By adopting a multilevel cooling flow channel structure based on interdigitated flow channels, cooling liquid with a large flow can be provided for transferring reflection face sedimentary hot under small water through pressure, pressure and flow of the cooling liquid inside each micro flow channel can be distributed comparatively uniformly, uniform cooling is realized on the reflection face, and over large thermal distortion of the large-diameter endoscope can be restrained. Adjacent second-level flow channels are communicated with the water inlet first-level flow channels and the water outlet first-level flow channels respectively and stacked with the third-level flow channels vertically, liquid does not need to flow through the whole section of the thin third-level flow channel, and flow resistance is greatly reduced.
Owner:DALIAN UNIV OF TECH

Self-similarity micro-channel heat sink with jet flow structure

The invention discloses a self-similarity micro-channel heat sink with a jet flow structure. The heat sink comprises a main inflow and outflow structure, a shunt layer, a jet flow pore plate layer, amicro-channel (overflow channel) layer and a top cover plate. A plurality of jet flow holes are formed in the jet flow pore plate layer below the shunt layer, and the forming positions are arranged along the flowing directions of shunt sub-channels. A sub-channel layer is positioned below the jet flow pore plate layer and is composed of a plurality of microgrooves arranged in parallel, and the intermittent micro-channel (overflow channel) structure is formed by the microgrooves and the bottom surface of the jet flow pore plate layer. A main inflow channel adopts a cross section reduced structure to guarantee uniform distribution of a cooling working medium towards the shunt sub-channels. The diameters of jet flow holes in the jet flow pore plate below the shunt layer are reduced along theflow, so that the micro-channels (overflow channels) below the shunt sub-channels obtain similar flow, and the uniformity of heat exchange is improved. The cooling working medium vertically impacts the bottom surfaces of the overflow channels after passing through the jet flow holes, a certain jet flow impact effect is formed, and heat transfer enhancement is achieved.
Owner:SICHUAN UNIV

Central flue system and uniform flow distribution method thereof

The invention discloses a central flue system. The central flue system comprises range hoods, an outdoor control system and a check valve control system, wherein an air outlet of each range hood is incommunication with a public flue through a respective smoke pipe, an adjustable check valve is mounted in each smoke pipe, a flue fan is mounted in the public flue, the range hoods are unpowered range hoods, the outdoor control system is used for controlling the rotating speed or frequency of the flue fan, the check valve control system is used for adjusting the opening angle of a valve plate ofthe adjustable check valve, and the check valve control system and the outdoor control system can communicate with each other. The invention further discloses a flow uniform distribution method of thecentral flue system, an extractor hood of the central flue system is an unpowered extractor hood, the rotating speed or frequency of the flue fan is adjusted through the outdoor control system, the opening angle of the valve plate is controlled through the check valve control system, the flow uniform distribution method only needs to preset the preset angles of the valve plate under two differentstarting rates, uniform flow distribution can be ensured through judgment of the startup rate, and the adjustment process is simple and efficient.
Owner:NINGBO FOTILE KITCHEN WARE CO LTD
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