Petal pore plate longitudinal-flow heat exchanger
A technology of heat exchanger and orifice plate, which is applied in the direction of heat exchanger type, indirect heat exchanger, heat transfer modification, etc. It can solve the problem of fluid flow performance that needs to be improved, heat transfer efficiency of heat exchanger is reduced, and flow resistance is increased and other problems, to achieve good anti-scaling and descaling functions, convenient processing, good anti-vibration and anti-vibration effects
Inactive Publication Date: 2009-10-07
ZHENGZHOU UNIV
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Problems solved by technology
The traditional shell-and-tube heat exchanger adopts a smooth circular tube and a single-bow baffle structure. The fluid flows in the shell side perpendicular to the axial direction of the tube, and there is a large heat transfer dead zone, which makes the overall heat exchanger Heat transfer efficiency decreases, flow resistance increases, and fluid-induced vibration often occurs at large Reynolds numbers, resulting in heat exchanger failure
Therefore, the shell-side tube bundle support structure and fluid flow performance of the shell-and-tube heat exchanger need to be improved
Method used
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Embodiment Construction
[0007] The structural processing of the petal orifice plate is still based on the full circular plate. After the tube holes are drilled, the hole bridge between the adjacent tubes is cut along the same direction and punched to one side to form a petal shape, so that the fluid between the tubes is longitudinal. Flow and wash the petals on the support strips of the orifice plates. During installation, the two petal orifice plates are arranged in a criss-cross pattern, and the support strips on the two orifice plates are used to realize all-round constraints on the heat exchange tubes.
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The invention relates to a longitudinal-flow heat exchanger which takes a petal pore plate as bundle support; the heat exchanger comprises a shell body, a seal head, a heat transfer tube bundle, a petal pore plate support, a pull tube and a tube spacer, a shell-side inlet and outlet tube, a tube-side inlet and outlet tube, and the like, wherein the petal pore plate is shown as the attached drawing 1, i.e., an entire circular plate which is a full circular plate composed of support strips and pedals which are arranged along the same direction, and is a key component of the heat exchanger; by the support strips which are arranged in a criss-cross way on two petal pore plates, the all-round support to the heat exchanger bundle is achieved, thereby leading the whole bundle to have good vibration prevention and resistance capacity; under the action of the petal pore plate, the heat exchanger shell-side fluid flows vertically along a tube axis; the functions of flow guide and disturbance of the pore plate petal can exacerbate fluid turbulence, thereby effectively enhancing convective heat transfer and producing good scale prevention and descaling functions; and the blocking effect of the periphery of the pore plate reduces the leakage flow ineffective on heat transfer; and the invention can be widely used in heat exchange equipment such as longitudinal-flow vertical and horizontal tube shell type heat exchanger, tube shell type condenser, etc.
Description
Technical field [0001] The invention relates to a novel longitudinal flow heat exchanger and its tube bundle support—petal orifice plate, which can support the heat exchange tube bundle and has a flow-disturbing effect, and the formed heat exchanger can effectively improve the heat transfer efficiency , and reduce shell side pressure drop, reduce power consumption, can be widely used in chemical industry, oil refining, light industry, energy and power and other heat exchange occasions. Background technique [0002] In the process industry, the heat exchanger is the key equipment to ensure the normal operation of the industrial system, the temperature of the process medium is reasonable, save energy and recover waste heat (or waste heat), and it occupies a large part of the entire project in terms of metal consumption, power consumption and investment. share. According to statistics, in general petrochemical enterprises, the investment of heat exchangers accounts for 40-50% ...
Claims
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Login to View More IPC IPC(8): F28D7/10F28F13/06
Inventor 吴金星魏新利王海峰朱登亮
Owner ZHENGZHOU UNIV
