CN202237786U - A Tangential Spiral Jet Wet Flue Gas Desulfurization Device - Google Patents

Abstract

The utility model discloses a tangent circle type spiral spraying wet flue gas desulfurization device, which comprises an absorption tower, wherein a tangent circle type spiral spraying turbulent flow absorption layer, a conventional spraying layer and a demisting layer are sequentially arranged in the absorption tower from bottom to top; the tangent circle type spiral jet turbulent flow absorption layer is composed of a plurality of groups of opposite-tangent circle ultrasonic atomizing nozzles which are arranged along a circular pipeline; the conventional spraying layer is composed of a plurality of mechanical nozzles arranged in an array; the high-efficiency atomizing nozzle is arranged on the tangent circle type spiral jet turbulent flow absorption layer to form a tangent circle type jet turbulent flow absorption field, and the generated atomized particles with the particle size of 50-400 mu m spirally rise, so that the mixing uniformity of reactants is enhanced, the contact time is prolonged, the absorption reaction speed is accelerated, and the desulfurization efficiency is improved; this patent can reduce the desulfurization liquid gas ratio, and the quantity of the atomizing nozzle that significantly reduces the desulfurizing tower volume, reduces desulfurization cost and energy consumption, but the wide application is in the wet flue gas desulfurization system of trades such as electric power, petrochemical industry, metallurgy, cement.

Description

A Tangential Spiral Jet Wet Flue Gas Desulfurization Device

technical field

The utility model relates to a flue gas desulfurization device, in particular to a tangential spiral spray wet flue gas desulfurization device.

Background technique

SO ₂ pollution is the main problem of air pollution in our country and an important environmental factor restricting the coordinated and stable development of our economy. With the rapid development of thermal power plants, _SO2 emissions are increasing. The emission of SO ₂ is one of the main reasons for the increasing acid rain. How to implement desulfurization projects in coal-fired power plants, improve desulfurization process, and improve desulfurization efficiency are effective means to effectively curb SO ₂ emissions. Lime/limestone-gypsum wet flue gas desulfurization technology is currently the most mature technology for controlling SO ₂ and has been widely used. However, there are also problems of low desulfurization efficiency, high energy consumption and high desulfurization cost.

In the wet desulfurization process, the core part is the desulfurization tower. In the desulfurization tower, the sulfur-containing flue gas is absorbed and oxidized. The main factors affecting desulfurization efficiency and energy consumption are desulfurization methods and devices.

At present, the effect of wet flue gas desulfurization in power plants is not good, and there are many defects. In order to improve the utilization rate of the slurry and ensure the desulfurization efficiency, on the one hand, it is necessary to build a large absorption tower and require the slurry pump to pump the slurry for spraying for multiple cycles; on the other hand, the spray layer of the absorption tower needs to install 2 to 4 layers of nozzles, Each layer requires more than 80 nozzles. Therefore, it needs to spend a lot of equipment construction, operation, maintenance, overhaul and other costs.

Therefore, in order to improve the desulfurization efficiency and ensure the efficiency of the absorption tower, the desulfurization absorption system should be improved and optimized. It is of great significance to design a set of wet flue gas desulfurization equipment scientifically and rationally.

Contents of the invention

In order to improve the desulfurization efficiency of the desulfurization system and reduce the cost of desulfurization, and ensure the safe, stable and economical operation of the wet flue gas desulfurization system, the utility model proposes a tangential spiral jet wet flue gas desulfurization device.

The utility model is realized through the following technical solutions:

A tangential spiral jet wet flue gas desulfurization device, including an absorption tower, is characterized in that a tangential spiral jet turbulent absorption layer, a conventional spray layer and a demister layer are sequentially arranged in the absorption tower from bottom to top; The tangential circular spiral jet turbulence absorbing layer is composed of multiple sets of ultrasonic atomizing nozzles arranged along the circular pipeline (but not limited to ultrasonic atomizing nozzles); the conventional spray layer is arranged in several arrays It consists of mechanical nozzles; the mist removal layer is a mist eliminator, and the bottom of the absorption tower is provided with a slurry storage area.

The multiple sets of punching circle ultrasonic atomizing nozzles arranged along the circular pipeline, wherein each group of punching circle ultrasonic atomizing nozzles form tangent circles with different diameters.

The multiple groups of punching and tangential circle ultrasonic atomizing nozzles arranged along the circular pipeline, wherein the same group of ultrasonic atomizing nozzles have the same downward inclination angle, and the inclination angle is 5°-15°.

The ultrasonic atomizing nozzle and the mechanical nozzle are respectively connected to the pipeline of the slurry storage area through the slurry pump.

The demisting layers are respectively connected to the clean water supply device through pipelines.

The slurry storage area is provided with an agitator and an oxidation fan, and the slurry storage area is also connected with a slurry replenishment system, which includes a slurry pump, a slurry tank, and an agitator.

The demister is a multi-layer demister, and multi-directional high-pressure flushing water nozzles are arranged between each layer of demisters.

The flue gas inlet of the absorption tower is arranged under the tangential spiral jet turbulent flow absorption layer, and the flue gas outlet of the absorption tower is arranged at the top or side of the end of the absorption tower.

Compared with the prior art, the beneficial effects of the utility model are:

1. The turbulent flow field generated by the tangential spiral jet turbulent absorption layer, and the desulfurization agent in the tangential spiral movement of different diameters fills the absorption tower, eliminating the dead corner of the desulfurization reaction, enhancing the mixing uniformity of the reactants, and speeding up the rate of the absorption reaction .

2. The ultrasonic atomizing nozzles of the tangential spiral jet turbulent absorption layer are arranged at an angle of 5°-15° downwards to prolong the contact time between the flue gas and the desulfurizer, so that the flue gas and the desulfurizer can fully react and improve desulfurization efficiency.

3. The tangential spiral jet turbulent absorbing layer, using the tangential arrangement of ultrasonic atomizing nozzles can greatly reduce the requirements for the atomization cone angle of the desulfurization nozzle, reduce the number of nozzles used, and reduce the volume of the desulfurization device accordingly, saving the desulfurization tower invest.

4. The tangential spiral jet turbulent absorption layer adopts the combination of tangential jet turbulent desulfurization and conventional wet desulfurization, and implements double desulfurization of flue gas, with high desulfurization efficiency, low desulfurization energy consumption and cost.

5. The tangential spiral jet turbulent absorption layer adopts ultrasonic atomizing nozzles, which greatly reduces the particle size of the atomized particles, increases the contact specific surface area of the reactants, and improves the desulfurization efficiency. It can reduce the number of slurry cycles and reduce the energy consumption of desulfurization.

Description of drawings

Fig. 1 is the structural representation of the utility model.

Fig. 2 is a schematic diagram of the structure of the circular tangential spiral jet turbulent flow absorbing layer in Fig. 1 .

Detailed ways

The specific implementation manner of the present utility model will be further described in detail below, but the implementation manner of the present utility model is not limited thereto.

As shown in Figure 1. The utility model tangential spiral jet wet flue gas desulfurization device includes an absorption tower, and in the absorption tower, there are sequentially arranged a tangential spiral jet turbulent absorption layer II, a conventional spray layer III and a demister layer from bottom to top. IV; the tangential spiral jet turbulence absorbing layer II is composed of multiple groups of ultrasonic atomizing nozzles 13 arranged along the circular pipeline to punch and cut circles; the conventional spray layer III is composed of several mechanical spray nozzles arranged in arrays Nozzle 2 composition;

as shown in picture 2. The multiple sets of punching and tangential circle ultrasonic atomizing nozzles 13 arranged along the circular pipeline, wherein each group of punching and tangential circle nozzles form tangential circles with different diameters. The multiple groups of punching and cutting circle ultrasonic atomizing nozzles 13 arranged along the circular pipeline, wherein the same group of ultrasonic atomizing nozzles 7 have the same downward inclination angle, and the inclination angle is 5°-15°.

The mist removal layer IV is a mist eliminator, which is a multi-layer mist eliminator, and multi-directional high-pressure flushing water nozzles are arranged between each layer of mist eliminators.

The bottom of the absorption tower is provided with a slurry storage area 1, the slurry storage area 1 is provided with an agitator 11, an oxidation blower 12, and the slurry storage area 1 is also connected with a slurry replenishment system, and the slurry replenishment system includes a slurry pump 9. Serous liquid filling 10. Stirrer 7.

The ultrasonic atomizing nozzle 13 and the mechanical nozzle 2 are respectively connected to the pipeline of the slurry storage area I through the slurry pump 8; the demisting layer IV is respectively connected to the clean water supply device through the pipeline 1, and the clean water supply device includes a pressure gauge 3. Regulating valve 4. High pressure flushing pump 5. Clean water tank 6.

The flue gas inlet 15 of the absorption tower is arranged under the tangential spiral jet turbulent flow absorption layer II, and the flue gas outlet 16 of the absorption tower is arranged at the top or side of the end of the absorption tower.

The working principle of the tangential spiral jet wet flue gas desulfurization device is as follows:

The slurry stored in the slurry tank 10 is transported to the slurry storage area I by the slurry pump 9 through a pipeline, and then, under the action of the slurry pump 8, is transported to the tangential spiral jet turbulent absorption layer II and conventional spraying Layer III. The slurry is sprayed from the ultrasonic atomizing nozzle 13 in the tangential spiral jet turbulence absorption layer II, and atomized particles are generated to contact the flue gas to realize the primary desulfurization of the flue gas; the slurry is sprayed in the conventional spray layer III by ordinary The mechanical nozzle 2 sprays to produce mist particles with larger particle size, which contacts with the flue gas to realize secondary desulfurization.

The slurry that has completed the desulfurization action descends under the action of gravity, etc., and gathers in the slurry storage area I again. The settled slurry and the newly prepared slurry from the slurry tank 10 are uniformly mixed under the action of the agitator 11 to realize recycling, and the intermediate reactants are oxidized under the action of the oxidation fan 12 .

The flue gas enters the tangential spiral jet turbulent flow absorption layer II from the flue gas inlet 15, and is evenly mixed with finer atomized particles to complete a desulfurization. Afterwards, the flue gas continues to move upwards to the conventional spray layer III, where the flue gas contacts with larger droplets in the region of the conventional spray layer III to complete the secondary desulfurization; the larger droplets simultaneously capture fine particles. After the primary and secondary desulfurization, the flue gas carries part of the mist droplets and continues to move upward to the demisting layer IV. After efficient demisting in the area of the demisting layer IV, the flue gas is discharged from the absorption tower through the flue gas outlet 16.

Among them, the cleaning medium of the demister layer IV is provided by the clean water tank 6 of the clean water supply device, and the high-pressure flushing pump 5, regulating valve 4, and pressure gauge 3 installed on the clean water pipeline are used to control the pressure and flow of the clean water.

As shown in Figure 2, the tangential spiral jet turbulent absorption layer II adopts ultrasonic atomizing nozzles 13, and the ultrasonic atomizing nozzles 13 are arranged tangentially along the circular pipeline 14 (the pipeline 14 is arranged along the inner wall of the absorption tower). , the jets of atomized particles ejected from the ultrasonic atomizing nozzles 13 arranged at different angles form tangential circles with different diameters along the circumferential direction; in the vertical direction, the atomized particles move downward due to inertia, stagnate due to the action of the smoke flow, and then the fog The fine particles move upwards with the airflow, forming a plurality of turbulent flow fields that first spiral downward and then spiral upward in the region of the tangential spiral jet turbulent flow absorption layer II. The number of layers of ultrasonic atomizing nozzles 13 is designed mainly according to the diameter of the absorption tower and the range of the adopted ultrasonic atomizing nozzles 13 (Fig. 2 takes the three-layer tangential circle arrangement as an example), so as to ensure that the entire absorption tower cross section is full of mist Granular desulfurization agent (limestone slurry) to avoid desulfurization dead ends.

Just can realize this patent preferably as mentioned above.

The above-mentioned embodiment is a preferred implementation mode of the present utility model, but the implementation mode of the present utility model is not limited by the above-mentioned embodiment, and any other changes, modifications and substitutions made without departing from the spirit and principle of the present utility model , combination, and simplification, all should be equivalent replacement methods, and are all included in the protection scope of the present utility model.

Claims (8)

1. A tangential spiral jet wet flue gas desulfurization device, including an absorption tower, is characterized in that a tangential spiral jet turbulent absorption layer, a conventional spray layer and a demisting layer are sequentially arranged in the absorption tower from bottom to top Layer; the tangential spiral jet turbulence absorbing layer is composed of multiple groups of ultrasonic atomizing nozzles arranged along the circular pipeline to punch and cut the circle; the conventional spray layer is composed of several mechanical nozzles arranged in arrays; The mist removal layer is a mist eliminator, and the bottom of the absorption tower is provided with a slurry storage area. 2. The circular tangential spiral spray wet flue gas desulfurization device according to claim 1, characterized in that said multiple sets of ultrasonic atomizing nozzles arranged along the circular pipeline for punching and tangential circles, wherein each group of punching and tangential circles The jets of ultrasonic atomizing nozzles form tangent circles of different diameters. 3. According to claim 2, said circular tangential spiral jet wet flue gas desulfurization device, characterized in that said multiple groups of ultrasonic atomizing nozzles arranged along circular pipelines, wherein the same group of ultrasonic atomizing nozzles The downward inclination angles of the nozzles are the same, and the inclination angles are 5° to 15°. 4. The tangential spiral jet wet flue gas desulfurization device according to claim 3, characterized in that the ultrasonic atomizing nozzle and the mechanical nozzle are respectively connected to the pipeline in the slurry storage area through a slurry pump. 5 . The circular tangential spiral jet wet flue gas desulfurization device according to claim 4 , wherein the demisting layers are respectively connected to the clean water supply device through pipelines. 6. According to claim 5, the tangential spiral jet wet flue gas desulfurization device is characterized in that the slurry storage area is provided with an agitator and an oxidation fan, and the slurry storage area is also connected with a slurry replenishment system. The slurry replenishment system includes a slurry pump, a slurry tank, and an agitator. 7. According to claim 6, the tangential spiral jet wet flue gas desulfurization device is characterized in that the demister is a multi-layer demister, and multi-directional high-pressure flushing water nozzles are arranged between each layer of demisters . 8. The tangential spiral jet wet flue gas desulfurization device according to claim 7, characterized in that the flue gas inlet of the absorption tower is arranged below the tangential spiral jet turbulent absorption layer, and the flue gas of the absorption tower The gas outlet is arranged on the top or side of the end of the absorption tower.

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