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Inner sleeve plate structure for plate-type fractionating tower

A technology of fractionation towers and sets of plates, applied in the direction of fractionation, etc., can solve problems such as non-elimination, achieve the effects of preventing coking, improving mass transfer efficiency, and reducing residence time

Active Publication Date: 2015-05-13
CHINA PETROCHEMICAL CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This patent does not have the functions of eliminating the stagnation area of ​​the tray, adapting to the change of the gas-liquid load in the fractionation column, improving the process performance and separation efficiency of the tray plate, and failing to effectively prevent heavy, inferior, and heat-sensitive materials from being trapped in the tray plate. Pyrolysis, polymerization, coking, fouling, clogging, etc.

Method used

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  • Inner sleeve plate structure for plate-type fractionating tower
  • Inner sleeve plate structure for plate-type fractionating tower
  • Inner sleeve plate structure for plate-type fractionating tower

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Embodiment

[0039] as attached Figure 4 As shown, according to the vapor-liquid load and the nature of the system in the fractionation tower, the 1# to 3# layer trays need to be installed with inner sleeves to eliminate the stagnation zone. The inner sleeve plate 4 of the plate type fractionation column of the present invention is arranged to cover the 1#~3# layer trays. The top of the inner casing plate is not lower than the liquid layer height on the 3# tray plate, and the bottom edge is lower than the 1# tray plate; the top of the inner casing plate is blocked by the top cover plate 5, and the lower part is open.

[0040] attached Figure 4 , Figure 5 In the application example, the inner sleeve plate 4 is composed of three inner sleeve plate combination plates 4-1, 4-2, 4-3, and the three inner sleeve plate combination plates are connected by bolts; the inner sleeve plate 4 and The top cover plate 5, the top cover plate 5 and the top cover plate supporting plate 8 are connected b...

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Abstract

The invention relates to an inner sleeve plate structure of a plate-type fractionating tower. The inner sleeve plate structure comprises a group of column trays and down-flow plates arranged in the tower normally; the down-flow plates are cooperated with the inner sleeve plate structure; the down-flow plates and liquid-receiving trays are disposed on every layer of the column tray; the down-flow plates is fixedly connected or boltedly connected with a down-flow plate connecting plate; and the down-flow plate connecting plate is connected with the inner wall of the tower. The inner sleeve structure comprises at least one inner sleeve plate; and the inner sleeve plate structure is arranged along a tower height direction; namely, at least one inner sleeve plate is fixed in the tower along the wall of the plate-type fractionating tower. The inner sleeve plate structure is used for changing an overflowing area of the liquid-receiving trays. The inner sleeve plate structure can eliminate viscous flow areas of the column trays, is adaptive to gas-liquid load changes in the tower, increases process performance of the fractionating tower, increases liquid flow speed on the column tray plates; eliminates viscous flow of the liquid, and effectively prevents heavy, poor and heat-sensitive materials from phenomena such as cracking, polymerizing, coking, scaling, blocking and the like on the column trays.

Description

technical field [0001] The invention relates to an internal part of a fractionation tower, in particular to an inner sleeve plate structure of a plate type fractionation tower. Background technique [0002] As an important mass transfer and separation equipment in petroleum, petrochemical, pharmaceutical and other fields, plate fractionation column is widely used. Tray column internals mainly include tray plates, downcomers, feed distributors (distributors), oil collection tanks, gas distributors, liquid extraction and other structures. As the main internal member, the tray plate is divided into three types: bubbling type, jet type and mixed type. Regardless of the type, the basic structure of the tray plate is as follows figure 1 As shown, it is mainly composed of bubbling area (a, f), downcomer area b, liquid distribution area c, foam breaking area d and invalid area e. Due to the circular structure of the fractionation column, there is a stagnation zone f in the bubbli...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D3/18
Inventor 王亚彪袁毅夫王秋萍
Owner CHINA PETROCHEMICAL CORP
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