Active centrifugal gas-liquid separation device

A gas-liquid separation device, active technology, applied in the field of liquid separation and recovery, gas field, can solve the problems of decreased separation efficiency, high maintenance cost, large flow of washing liquid, etc., to relax the oxygen content range, reduce maintenance costs, reduce The effect of maintenance costs

Inactive Publication Date: 2012-07-18
杨东进
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Disadvantages: low separation efficiency, bulky equipment, occupying a lot of space, when the diameter of liquid particles in wet gas is small, the separation efficiency drops sharply
2) If two or more particles are thrown into one hole at the same time, bridging phenomenon will also occur
Disadvantages: the processing gas volume is small, the applicable gas liquid content is also small, it is very easy to block, the resistance is high, and it is not suitable for viscous liquid or medium containing solid particle impurities
Disadvantages: large flow of washing liquid, complex system, high energy consumption and high maintenance costs
Disadvantages: high-voltage electrostatic device is required, the system is complex, high energy consumption, high cost, high maintenance cost, and there is a strict limit on the oxygen content of the mixed gas for separating flammable liquid particles, otherwise there is a risk of explosion
However, the separation efficiency of the improved centrifugal gas-liquid separator is

Method used

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  • Active centrifugal gas-liquid separation device
  • Active centrifugal gas-liquid separation device
  • Active centrifugal gas-liquid separation device

Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0061] Example 1

[0062] Refer to figure 1 As shown, an active centrifugal gas-liquid separation device adopts a vertical arrangement scheme, which mainly includes a casing 1, a rotating drum 2, a power unit 3, a partition plate 4, an intake pipe 5, an exhaust pipe 6, and a liquid discharge pipe 7. Frame 8. The diameter of the drum is 1m, and the rotation speed is 2500r / min. The shell 1 made of steel plate is set on the frame 8. The shell 1 is provided with a rotating drum 2, and the rotating drum 2 is made of steel pipe. A large number of vents, the inner space of the cylinder and the outer space of the cylinder are connected through vents; the drum 2 is connected to the power unit 3 through the cylinder cover 21 and the shaft 22 with vents. The power unit 3 includes a motor and a coupling through which the drum 2 passes The shaft 22 and the bearing are supported on the bearing seat and rotate around its own axis driven by the power device 3. The drum 2 is provided with a pa...

Example Embodiment

[0065] Example 2

[0066] Refer to figure 2 As shown, an active centrifugal gas-liquid separation device adopts a horizontal arrangement scheme, and the drain pipe 7 is arranged at the lowest part of the housing 1, and the rest is the same as in Embodiment 1.

Example Embodiment

[0067] Example 3

[0068] Refer to image 3 , Figure 4 As shown, an active centrifugal gas-liquid separation device adopts a vertical arrangement. The intake pipe 5 is located at the lower end of the housing 1, the exhaust pipe 6 is located at the upper end of the housing 1, and the cylinder wall at the intake end of the drum 2 is provided with multiple A centrifugal blade 23, a plurality of centrifugal blades 23 and the rotating drum 2 together constitute a centrifugal turbine impeller. When the rotating drum 2 rotates, a certain wind pressure can be provided to promote the gas flow. ω is the rotating direction of the rotating drum 2 in the figure. The rest is the same as in Example 1.

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PUM

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Abstract

The invention is applied in the industries of medicine, air compression, natural gas, synthetic ammonia, oil refining, coking and the like, and relates to a gas-liquid separation device. The device comprises a shell, an air inlet pipe and an exhaust pipe; a drum driven to rotate by a power device is arranged in the shell; the wall of the drum is provided with air holes; a partition plate is arranged in the drum to partition the drum into an air inlet end and an exhaust end which are respectively communicated with the air inlet pipe and the exhaust pipe; the air inlet pipe is communicated with the exhaust pipe through the air inlet end of the drum, the air holes in the wall of the drum, an air passage and the exhaust end of the drum; and the shell is provided with a drain pipe. Through the device, the separation efficiency of liquid particles with the diameters of over 0.1 micron reaches over 99.5 percent; and the device is large in treated gas quantity and suitable for wet gas with high liquid content, does not require circulation of a large quantity of washing absorption liquid, does not require a high-voltage electrostatic system, has good adaptability to the physical properties of the liquid, has certain capability of separating dry gas components with different densities, and is small in volume, light in weight, small in occupied space and low in manufacturing cost.

Description

technical field [0001] The invention belongs to the technical field of gas and liquid separation and recovery, and relates to a gas-liquid separation device. Background technique [0002] Gas-liquid separation refers to a process of separating dry gas and liquid particles in gas-liquid two-phase mixed wet gas containing suspended tiny liquid particles. It is widely used in medicine, air compression, natural gas supply, synthetic ammonia, oil refining, coking, etc. industry. The suspended tiny liquid particles contained in the wet gas are generally distinguished by the size of the liquid particle diameter. Usually, when the liquid particle diameter is less than 10 μm, it is called "fog", and when the liquid particle diameter is within 10 μm to 1000 μm, it is called "fog". ", greater than 1000μm, it is called a "droplet". [0003] The formation mechanisms of "fog" and "foam" in the airflow usually include: mechanical action, steam condensation, and chemical reaction. The d...

Claims

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Application Information

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IPC IPC(8): B01D45/14
Inventor 杨东进
Owner 杨东进
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