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A high throughput tray tower

A plate tower, high-throughput technology, applied in the field of plate fractionation or rectification tower, plate tower internals structure, can solve the problem of affecting the operation flexibility and separation efficiency, reducing the liquid flow intensity of the tray plate, and reducing the mass transfer efficiency. , to achieve the effects of improving mass transfer efficiency and processing capacity, expanding the range of bubbling area, reducing liquid surface gradient and liquid layer thickness

Active Publication Date: 2015-09-02
袁小明
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, although the special structure of the suspended downcomer increases the area of ​​the bubbling area of ​​the tray, it affects the operating flexibility and separation efficiency; The processing capacity of the liquid load, but the short flow of the liquid on the tray plate also affects the mass transfer efficiency
Therefore, although the MD plate column technology can effectively improve the processing capacity of the high liquid load fractionation column, the mass transfer efficiency will be slightly reduced, and the operating flexibility will be greatly affected

Method used

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  • A high throughput tray tower
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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] The plate tower internals are located inside the tower shell 5 and are arranged in a stacked structure. Each layer includes a tray plate 1, a downcomer 7, and a liquid receiving plate 4. That is, one end of each tray plate is connected to the liquid receiving plate, and the other end is connected to the liquid receiving plate. To the downcomer, the tray plate of the lower layer corresponds to the tray plate of the upper layer, and the liquid receiving plate of the lower layer corresponds to the downcomer setting of the upper layer, arranged layer by layer. This structure is the prior art.

[0047] Such as image 3 , 4 , 5, a high flux tray tower, the tray plate 1 is inclined downward along the liquid flow direction, that is, the end connected to the liquid receiving tray is the upper end of the tray plate 1, and its The end communicating with the downcomer is the lower end of the tray plate 1 . The angle a between the tray plate and the horizontal line is 3°-45°. The...

Embodiment 2

[0055] Such as Figure 6 As shown, a high-throughput tray column, the tray column internals are located inside the column shell, including tray plates, downcomers, and liquid receiving trays. A total of 117 trays are installed in the plate fractionation tower. According to the vapor-liquid load and the nature of the system in the fractionation tower, the tower diameter Ф6600mm, 8 liquid flow high-flux plate tower structure technology is adopted through hydraulic calculation. The tray plate 1 is inclined downward along the liquid flow direction, that is, the upper end of the tray plate 1 is connected to the liquid receiving tray, and the lower end of the tray plate 1 is connected to the downcomer. . In the middle part of the tray tower, the upper ends of the two opposite tray plates 1 are connected by the liquid receiving tray 4, and the lower ends of the two opposite tray plates 1 form the inlet of the downcomer 7; The upper end of a tray plate 1 is connected to the tower sh...

Embodiment 3

[0060] Such as Figure 7 , a high-throughput tray tower, the tray tower internals are located inside the tower shell 5, including a tray plate, a downcomer, and a liquid receiving tray, and the tray plate 1 is inclined downward along the liquid flow direction, that is, The upper end of the tray plate 1 is connected to the liquid receiving tray, and the lower end of the tray plate 1 is connected to the downcomer. The included angle between the tray plate 1 and the horizontal is 45°. The main function of the inclined tray plate is to improve the liquid flow state on the tray plate, reduce the thickness of the liquid layer, increase the length of the liquid flow and the area of ​​the bubbling area. In the middle of the tray tower, the lower ends of two opposite tray plates form the inlet of the downcomer 7, and the width of the inlet is 100 mm. The tray plate is not provided with an outlet weir, because setting the outlet weir will affect the beneficial effect of the inclined t...

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Abstract

The invention discloses a high-flux plate-type tower. A tray plate is inclined downwards along the liquid flowing direction. A gas guide plate is fixed below the tray plate, and is obliquely arranged, and the inclination direction of the gas guide plate is opposite to that of the tray plate. A down-flow plate of a down-flow pipe is obliquely arranged, and is arranged below the gas guide plate, the upper end of the down-flow plate is fixedly connected with the gas guide plate, and a gap is formed between the lower end of the down-flow plate and a lower liquid receiving disc. The structure of the high-flux plate-type tower can be used for a single-overflow, double-overflow or multi-overflow plate-type tower. By inclining the tray plate, the liquid runner is lengthened, and the area of a bubbling region is increased; by changing the liquid flowing state on the tray plate, the gradient of a liquid surface and the thickness of a liquid layer can be reduced, the pressure drop is reduced, and the transferring efficiency and the machining capacity can be improved. By installing the gas guide plate, the flowing direction of the airflow ascending from the lower tray can be changed, the length of the runner is increased, the mist foam can be reduced, and the operation upper limit of the tray plate can be improved. By adopting the oblique down-flow plate, the volume of the down-flow pipe is increased.

Description

technical field [0001] The invention relates to a plate type fractionation or rectification tower, in particular, relates to a plate type tower internal part structure, which is mainly used in technical fields such as petroleum and petrochemical industry, environmental protection, food and medicine. Background technique [0002] As an important mass transfer and separation equipment in petroleum, petrochemical, pharmaceutical and other fields, plate fractionation / rectification tower is widely used. Tray column internals mainly include tray plates, downcomers, feed distributors or distribution pipes, oil collection tanks, gas distributors, liquid extraction and other structures. Tray plates and downcomers are the main internal components of the plate column, and their type and structure determine the processing capacity and product separation accuracy of the plate column. Over the years, the development of mass transfer and separation technology has driven the progress of va...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D3/14
Inventor 潘革波
Owner 袁小明
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