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Flow turning-back gas liquid cross-flow super-gravitational field revolving bed equipment

A high-gravity field and baffle-type technology, applied in chemical/physical/physical-chemical mobile reactors, fractionation, etc., can solve problems such as inefficient use of space, small gas circulation area, and small gas-liquid flow, etc., to achieve The effects of reduced energy consumption, reasonable structure, and improved mass transfer capacity

Active Publication Date: 2008-07-30
ZHEJIANG UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the rotating bed has a high mass transfer capacity, it also has its own weaknesses. Because the rotor adopts a structure combining dynamic and static parts, the liquid has experienced multiple static-acceleration processes in the rotor, so the energy consumption of the rotor rotation On the other hand, since half of the space inside the rotor is a non-mass transfer area, the flow area of ​​the gas inside the rotor is small, and the resistance of the gas in the rotor is large, so the gas pressure drop of the equipment is large
In addition, there are mass transfer and non-mass transfer areas inside the rotor of the baffled high-gravity field rotating bed, so the space in the rotor is not effectively utilized, so the gas-liquid flow rate is relatively small under the same equipment volume conditions

Method used

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  • Flow turning-back gas liquid cross-flow super-gravitational field revolving bed equipment
  • Flow turning-back gas liquid cross-flow super-gravitational field revolving bed equipment
  • Flow turning-back gas liquid cross-flow super-gravitational field revolving bed equipment

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] Embodiment 1: single-layer structure

[0018] As shown in Figure 1 and Figure 2, this baffle type gas-liquid cross-flow type supergravity field rotating bed device mainly includes a shell 1, a lower end plate 2, a lower concentric ring 3, a gas inlet 4, an upper concentric ring 5, Upper end plate 6 , gas outlet 7 , catheter 9 , liquid distributor 10 , liquid inlet 11 , liquid outlet 12 and rotating shaft 13 . The housing 1 is divided into an upper chamber 21 and a lower chamber 22 by a partition plate 23. The housing 1 is provided with a gas inlet 4, a liquid outlet 12, a gas outlet 7 and a liquid inlet 11, wherein the gas outlet 7 and the liquid inlet 11 The gas inlet 4 and the liquid outlet 12 communicate with the lower cavity 22 respectively. The rotating shaft 13 runs through the housing 1, and the rotor is composed of an upper end plate 6 fixedly connected with the rotating shaft 13, a lower end plate 2, an upper concentric ring 5, a lower concentric ring 3, and a...

Embodiment 2

[0021] Embodiment 2: multi-layer structure

[0022] As shown in Figure 3, the housing 1 is divided into an upper cavity 21, a second-layer intermediate cavity 24 and a lower cavity 22 by a partition plate 23, and the intermediate cavity 24 is provided with an intermediate feed port 15 to form a multi-layer baffle structure. Multiple rotors are coaxially connected in series in a single housing. The gas-liquid flow in each rotor is the same as that of a single-layer structure. The difference is that the gas leaving the center of a rotor will enter the outer edge of the adjacent upper rotor again, and then After passing through the upper rotor along the zigzag path, it enters another rotor above it; the liquid leaving this rotor is collected and enters the distributor 10 of the next rotor through the duct 9 of the adjacent rotor, Under the action of centrifugal force, it passes through the next layer of rotors and then enters the next layer of rotors. In this way, in the struct...

Embodiment 3

[0023] Embodiment 3: single-layer or multi-layer structure

[0024] As shown in Figure 4, when applied to gas-liquid mass transfer occasions, the last baffle area experienced by the gas at the center of each layer of rotor can be filled with packing 16, which can effectively prevent mist entrainment.

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PUM

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Abstract

The invention relates to a rotating bed of overweight field of baffled gas-liquid cross flowing type. The shell of the invention is divided into an upper cavity and a lower cavity by a separating plate; a sealing device is arranged between the separating plate and the upper end plate; a gas outlet and a liquid inlet are respectively communicated with the upper cavity; the gas inlet and the liquid outlet are respectively communicated with the lower cavity; a rotary shaft goes through the shell; the rotor consists of the upper end plate, a lower end plate, an upper concentric circle, a lower concentric circle and a liquid distributor which are fixedly connected with the rotary shaft, wherein, the upper concentric circle and the lower concentric circle are crossly positioned in the rotor to form a devious S-shaped baffled passage; the upper concentric circle and the lower concentric circle are provided with the small holes corresponding to the liquid outlet holes on the liquid distributor in axial direction; the gas inlet and the liquid outlet are communicated with the S-shaped passage; one end of a liquid guide pipe is communicated with the upper end of the liquid distributor while the other end with liquid inlet. The invention has the advantage of excellent mass transfer capability which reduces the rotational energy consumption and pressure.

Description

technical field [0001] The invention relates to a gas-liquid contact mass transfer device, in particular to a baffled gas-liquid cross-flow type supergravity field rotary bed device, which can be widely used in chemical, pharmaceutical, metallurgy, light industry and other industries for absorption, Occasions such as rectification, heat transfer, chemical reaction, and preparation of nanomaterials are especially suitable for gas absorption processes due to the extended path of the gas phase. Background technique [0002] Since its birth in the 1970s, hypergravity technology has been favored because it can greatly reduce the size of equipment. The earliest authorized patent on high-gravity technology is Professor Ramshaw's European patent EP0002568, the patent name is Mass transfer apparatus and its use, which discloses a packing type high-gravity field rotating bed (rotating packed bed), and many high-gravity technology later Patents such as ZL97212054.8, CN95214611.8, etc....

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J19/28B01D3/30
Inventor 计建炳徐之超王广全俞云良
Owner ZHEJIANG UNIV OF TECH
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