CN110575737B

CN110575737B - Array type pressurization water separating device

Info

Publication number: CN110575737B
Application number: CN201910972947.1A
Authority: CN
Inventors: 贾霄; 孙虹; 崔湘溁; 赵旭东
Original assignee: China Shenyang Jingxin Environmental Protection Technology Co ltd; Dalian University of Technology
Current assignee: China Shenyang Jingxin Environmental Protection Technology Co ltd; Dalian University of Technology
Priority date: 2019-10-14
Filing date: 2019-10-14
Publication date: 2021-12-03
Anticipated expiration: 2039-10-14
Also published as: CN110575737A

Abstract

The invention belongs to the technical field of wet scrubbing post-treatment in the chemical industry, and provides an array type pressurization water separation device. The array type pressurized water separation device is characterized in that an array type Venturi structure is additionally arranged in a flue gas pipeline, so that the gas pressure in a local area in the flue gas pipeline is increased, and gaseous water is separated out and flows down in a converged manner; the array type Venturi structure is arranged in a multilayer distribution mode and comprises a central water separating passage, a plurality of outermost ring passages and a plurality of middle passages located between the central water separating passage and the outermost ring passages. The invention can separate out the gaseous water in the wet flue gas and collect and discharge the gaseous water in the actual work, can truly remove the gaseous water, does not need heat exchange, and greatly saves energy consumption.

Description

Array type pressurization water separating device

Technical Field

The invention belongs to the technical field of wet scrubbing post-treatment in the chemical industry, and particularly relates to a device for separating and dehydrating gaseous water in flue gas, in particular to an array type pressurization water separating device.

Background

The flue gas discharged in industrial production has certain discharge requirements to prevent and control atmospheric pollution, and sulfur dioxide is one of common pollution emissions in chemical production. In order to control the emission amount of sulfur dioxide within a certain range, a wet desulphurization technology is usually adopted, flue gas is introduced into a washing tower, a liquid desulfurizer (such as limestone slurry) is used for absorbing sulfur dioxide in the flue gas, but the water content (gas state and liquid state) of tail gas subjected to the wet desulphurization technology is up to 20%, the flue gas can be gathered into liquid drops on the wall of a flue pipe to cause a rain drop phenomenon, the wall of the flue pipe and even a fan are corroded, a wet desulphurization system is stopped, and even the whole unit can be stopped. The common solution for flue gas dehydration is a corrugated plate demister, and the efficiency of separating and recovering liquid water can reach 50%. The principle of dehydration in the flue is that the fine liquid drops are mainly acted by the gravity and the blowing-supporting force of the airflow in the ascending airflow. When the blowing force of the air flow is smaller than the gravity of the liquid drops, the liquid water can be separated and recovered by the gravity. However, when the gas velocity is increased to a certain velocity, the carrying capacity of the particles is enhanced, a large amount of fine droplet particles are not easily removed, and the gas flow destroys a liquid film formed on the wall surface of the blade, causing secondary water entrainment, thereby lowering the dehydration efficiency. And the defroster can't separate the gaseous state water of mixing, can cause great pressure loss moreover, even cause the flue to block up. The method commonly used in the gaseous water industry is to heat the flue gas in the pipeline to improve the water content of the gas, so that the water-containing flue gas still does not reach a saturated state after the gas is cooled by a flue, thereby avoiding a large amount of white smoke at the outlet of the pipeline, but the method does not actually remove the water in the flue gas.

Chinese patent application No. CN204619695U discloses a high efficiency flue gas dewatering device which utilizes a condensation method to cool the flue gas to below the dew point rapidly, and the gaseous water in the flue gas can be condensed and separated out. Then the liquid water is collected and discharged by using a water collecting device, and the contact area between the flue gas and the refrigerating block is enlarged through the air passage improvement. The method can effectively separate out and remove the gaseous water, but the method has the defects of difficult guarantee of heat exchange efficiency, poor water removal effect and higher energy consumption.

Disclosure of Invention

Aiming at the defects in the prior art, the invention provides a design scheme of an array type pressurization water separation device, which utilizes a mechanical structure design, reduces the carrying capacity of gaseous water in a physical mode to separate out liquid water, considers the pressure loss condition of the device, saves a large amount of energy consumption under the condition of ensuring the integral pressure drop of the device, and removes water in smoke.

The technical scheme of the invention is as follows:

an array type pressurization water separation device is characterized in that an array type Venturi structure is additionally arranged in a flue gas pipeline, so that the gas pressure in a local area in the flue gas pipeline is increased, gaseous water is separated out and flows down in a gathering manner; the array type Venturi structure is arranged in a multilayer distribution mode and comprises a central water separating passage, a plurality of outermost ring passages and a plurality of middle passages positioned between the central water separating passage and the outermost ring passages; for the flue gas passage with the pipe diameter D, the inlet diameter of the central water separation passage is D1, the inlet diameter of the outermost ring passage is D2, the inlet diameter of the middle passage is D3, the arrangement mode of the gas passages is set according to the gas velocity distribution in the pipeline, and the simulation of the flue without the device shows that the gas velocity is higher in the central area and the wall surface area of the flue, so that the pressure loss is prevented from being too large, the diameters of the central passage and the outermost ring passage are set to be larger, namely D1 > D2 > D3. Meanwhile, in order to ensure the influence of the invention on the permeability of the flue gas in the pipeline, the requirements of D1+ D2+ D3 are less than 0.8D.

The gas passage in the pressurized water separation device adopts a Venturi structure to improve local gas pressure through the change of the diameter of the passage, the water carrying amount of saturated wet flue gas is gradually reduced along with the increase of the pressure, and when the pressure of the flue gas is improved to 0.2MPa, the water content is greatly reduced, so that the local gas pressure is improved to 0.2MPa through the diameter design of the passage. To achieve this goal, the throat diameter of the venturi structure is 0.49 of the inlet diameter, i.e. D1 ═ 0.49D1, D2 ═ 0.49D2, and D3 ═ 0.49D3, and to ensure the energy loss of flue gas, the length of the throat is 0.6 of the total length of the venturi structure.

The pressurized water separation device plates a layer of high molecular hydrophobic material on the Venturi type gas passage, and the high molecular hydrophobic material used in the scheme can change the surface property of the plated material, can promote the condensation of separated water and then is collected and discharged.

The invention has the beneficial effects that: the invention can separate out the gaseous water in the wet flue gas and collect and discharge the gaseous water in the actual work, can truly remove the gaseous water, does not need heat exchange, and greatly saves energy consumption.

Drawings

FIG. 1 is a schematic view of the structure of the present invention.

Fig. 2 is a side view of the present invention.

Fig. 3 is a schematic view of a flow field simulation.

In the figure: d1 inlet diameter of central water separation passage; d2 inlet diameter of outermost ring channel; d3 entrance diameter of intermediate passage; d1 throat diameter of central water-separating passage; d2 throat diameter of outermost ring pass; d3 throat diameter of the intermediate passageway.

Detailed Description

The following examples are given for the detailed implementation and specific operation of the present invention, but the scope of the present invention is not limited to the following examples.

As shown in fig. 1, an isometric model of an array type pressurized water separation device is prepared by pretreating an internal gas path of the device with acetone, quickly drying in air, and spraying a high-molecular hydrophobic material. The array structure of the passages of the pressurized water separation device adopts a 3-layer distribution arrangement mode, and for a flue gas passage with the pipe diameter of D, the diameter of the inlet of a central passage is D1, and the diameter of a throat pipe is D1; the diameter of the outermost ring passage is D2, and the diameter of the throat pipe is D2; the intermediate passage is D3 with a throat diameter D3.

Wherein:

D＝209mm；

D1＝60mm；

D2＝40mm；

D3＝20mm；

d1＝29.5mm；

d2＝19.2mm；

d3＝9.5mm；

results of the implementation

In the above embodiment, after the pressurized water absorption device is additionally arranged, the gaseous water can be effectively removed, when the ambient temperature is 44-55 ℃, the device raises the flue gas pressure in the passage to 0.2MPa, and at the moment, the water carrying capacity of the wet flue gas is shown in table 1, and the water removal efficiency can reach 68.6%.

TABLE 1 saturated humid air water content (g/kg dry air) at different pressures and temperatures

Claims

1. An array type pressurization water separation device is characterized in that an array type Venturi structure is additionally arranged in a flue gas pipeline, so that gas pressure in a local area in the flue gas pipeline is increased to separate out gaseous water and the gaseous water is collected and flows down; the array type Venturi structure is arranged in a multilayer distribution mode and comprises a central water separating passage, a plurality of outermost ring passages and a plurality of middle passages positioned between the central water separating passage and the outermost ring passages; for the flue gas passage with the pipe diameter D, the diameter of the inlet of the central water separation passage is D1, the diameter of the inlet of the outermost ring passage is D2, the diameter of the inlet of the middle passage is D3, and D1 is ensured to be more than D2 and more than D3; meanwhile, the requirements of D1+ D2+ D3 are less than 0.8D;

the throat diameter of the array type venturi structure is 0.49 of the inlet diameter, namely D1 is 0.49D1, D2 is 0.49D2, and D3 is 0.49D3, and meanwhile, in order to ensure the energy loss of smoke, the length of the throat is 0.6 of the total length of the venturi structure.

2. The array pressurized water separation device of claim 1, wherein the passages of the array venturi structure are coated with a layer of hydrophobic polymer material.