Reutilization device for residual oxidation air of desulfurization solution
By designing a desulfurization solution oxidation air allowance reuse device, and using the combination of the main air pipe, distribution pipe and aeration pipe, the problems of large air volume loss and sulfur deposition of the Roots blower are solved, efficient utilization of oxidized air and avoiding sulfur deposition are achieved, and the stability and economicality of the desulfurization device are improved.
Patent Information
- Application Number
- CN202421366733.2
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-06-14
- Publication Date
- 2025-05-06
- Estimated Expiration
- 2034-06-14
AI Technical Summary
During the oxidation and regeneration of the desulfurization solution, the wind volume loss is large, the wind energy loss rate is high, and sulfur deposition causes frequent damage to the agitator and long maintenance cycle, which seriously affects the stable operation of the desulfurization device.
A desulfurization solution oxidation air allowance reuse device is designed. Through the main air pipe recovery, distribution pipe adjustment and aeration pipe blowing, the surplus air volume of the Roots blower is evenly distributed in the sulfur foam tank, and the liquid is stirred through the air pressure and flow rate to avoid sulfur deposition.
It realizes efficient utilization of oxidized wind of Roots blower, reduces wind energy waste, reduces sulfur deposition, extends the service life of the equipment, reduces maintenance costs, and improves the stable operation of the desulfurization device.
Smart Images

Figure CN222829372U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of wet desulfurization, in particular to a desulfurization solution oxidation wind surplus recycling device. Background Art
[0002] The complex iron desulfurization process is mainly used for the desulfurization of low-yield, low-sulfur gas wells. During the oxidation regeneration process of the desulfurization solution, the Roots blower is used to blow oxygen into the flotation chamber to ensure that the Fe 2+ Maximum conversion to Fe 3+ During the operation, the Roots blower had a large air volume loss, with a wind energy loss rate of up to 35.68%. The mixer accessories and pumps were damaged frequently, and the agitator was damaged 14 times due to sulfur deposition, accounting for 70%. The high induction frequency, long maintenance cycle and high maintenance cost seriously restricted the stable operation of the desulfurization device in a safe, stable, long, full and excellent manner.
[0003] Therefore, there is an urgent need for a desulfurization solution oxidation air surplus recycling device to improve the utilization rate of the Roots blower oxidation air. Utility Model Content
[0004] In order to solve the above technical problems, the utility model proposes a desulfurization solution oxidation wind surplus recycling device to solve the production problems of Roots blower oxidation wind waste and sulfur foam tank sulfur deposition blockage.
[0005] The utility model provides a desulfurization solution oxidation wind surplus recycling device, comprising a Roots blower, wherein the vent of the Roots blower is connected to a main air pipe, the main air pipe is provided with multiple stages of distribution pipes connected to the main air pipe, and the other ends of the distribution pipes are respectively provided with aeration pipes.
[0006] In one embodiment, a regulating valve is provided on the distribution pipe to adjust the air intake volume of each stage of the distribution pipe.
[0007] In one embodiment, the aeration tube is a cross aeration tube.
[0008] In one embodiment, the distribution pipe and the aeration pipe are located on the same center line.
[0009] In one embodiment, the vent of the Roots blower is connected to the main air pipe via a connecting flange.
[0010] In one embodiment, the aeration pipe is placed in a sulfur foam tank.
[0011] In one embodiment, the diameter of the main air pipe is DN40-DN60, the diameter of the distribution pipe is DN10-DN30, and the diameter of the aeration pipe is
[0012] In one embodiment, the distance between adjacent distribution pipes is 1.0 to 1.8 meters.
[0013] In one embodiment, the distribution pipes are provided in 6 groups.
[0014] In one embodiment, the regulating valve is disposed above the observation hole of the sulfur foam tank.
[0015] Compared with the prior art, the desulfurization solution oxidation air surplus recycling device of the utility model evenly distributes the surplus air of the Roots blower in the sulfur foam tank through main air pipe recovery, distribution pipe adjustment and aeration pipe blowing and stirring, and stirs the liquid in the sulfur foam tank by air pressure and flow to avoid sulfur deposition, while realizing the recycling of the surplus air of the Roots blower, reducing wind energy waste, reducing costs and creating benefits.
[0016] The above-mentioned technical features can be combined in various technically feasible ways to produce new implementation schemes, as long as the purpose of the present utility model can be achieved. BRIEF DESCRIPTION OF THE DRAWINGS
[0017] The present invention will be described in more detail below based on non-limiting embodiments and with reference to the accompanying drawings, wherein:
[0018] Figure 1 A schematic diagram of a desulfurization solution oxidation wind surplus recycling device according to the utility model is shown.
[0019] In the figures, the same components are indicated by the same reference numerals. The figures are not drawn to scale.
[0020] Wherein, the accompanying drawings are marked as follows:
[0021] 1. Roots blower; 2. Connecting flange; 3. Main air pipe; 4. Distribution pipe; 5. Regulating valve; 6. Aeration pipe; 7. Sulfur foam tank; 8. Motor; 9. Drive shaft; 10. Observation hole. DETAILED DESCRIPTION
[0022] The present invention will be further described in detail below in conjunction with the accompanying drawings and specific embodiments. It should be noted that, as long as there is no conflict, the various embodiments and features in the various embodiments of the present invention can be combined with each other, and the resulting technical solutions are all within the protection scope of the present invention.
[0023] The parts not described in the present invention can be realized by adopting or drawing on the existing technology.
[0024] like Figure 1As shown, the utility model shows a specific embodiment of a desulfurization solution oxidation air surplus recycling device, including a Roots blower 1, the vent of the Roots blower 1 is connected to the main air pipe 3, the main air pipe 3 is provided with multiple stages or multiple distribution pipes 4 connected to the main air pipe 3, and the other ends of the distribution pipes 4 are respectively provided with aeration pipes 6.
[0025] In this embodiment, the Roots blower 1 is used to provide a power source for surplus gas. The main air pipe 3 is connected to the vent of the Roots blower 1, and is used to recover the surplus gas of the Roots blower 1 and send it to the sulfur foam tank 7. The distribution pipe 4 is connected to the main air pipe 3, and is used to evenly distribute the surplus gas of the Roots blower in various areas in the sulfur foam tank 7. The aeration pipe 6 is connected to the distribution pipe 4 and is placed in the sulfur foam tank 7. The air holes on the aeration pipe 6 distribute the surplus gas distributed by the distribution pipe 4 to the sulfur foam tank 7, and the liquid in the sulfur foam tank is stirred by air pressure and flow to avoid sulfur deposition. The sulfur deposition in the sulfur foam tank can be reduced to below 0.2 meters by the blowing and stirring of the aeration pipe 6.
[0026] In an optional embodiment, a regulating valve 5 is provided on the distribution pipe 4 to adjust the air intake volume of each level of the distribution pipe 4. Figure 1 As shown, the regulating valve 5 may be optionally arranged above the observation hole 10 of the sulfur foam tank 7 to facilitate gas volume regulation.
[0027] In an optional embodiment, the aeration tube 6 may be a cross aeration tube.
[0028] In an optional embodiment, the distribution pipe 4 and the aeration pipe 6 are located on the same center line to facilitate uniform distribution of the surplus gas of the Roots blower in the sulfur foam tank.
[0029] In an optional embodiment, the vent of the Roots blower 1 is connected to the main air pipe 3 through the connecting flange 2 .
[0030] In an optional embodiment, the diameter of the main air pipe 3 is DN40-DN60, the diameter of the distribution pipe 4 is DN10-DN30, and the diameter of the aeration pipe 6 is
[0031] In a specific embodiment, the diameter of the main air pipe 3 is DN50 (i.e., diameter inch 2", the outer diameter of the pipe is 60.3 mm), the diameter of the distribution pipe 4 is DN20, and the diameter of the aeration pipe 6 is
[0032] In a specific embodiment, the main air pipe 3, the distribution pipe 4 and the aeration pipe 6 can all be made of stainless steel, such as 304 stainless steel.
[0033] In an optional embodiment, 4 to 6 groups of distribution pipes 4 are provided, and the spacing between adjacent distribution pipes 4 is 1.0 to 1.8 m. Optionally, the distance between the distribution pipes 4 is 1.5 m.
[0034] It should be pointed out that although this embodiment lists the specific diameter / diameter, quantity and setting position of each pipeline, it does not mean that the diameter / diameter and quantity of the pipeline are limited to these values. The specific size, quantity and setting position of the pipeline can be set according to actual needs.
[0035] like Figure 1 As shown, the motor 8 and the transmission shaft 9 in the figure constitute a stirring device. The stirring device can be replaced by setting the desulfurization solution oxidation wind surplus recycling device of the present application, thereby reducing the operation of the motor. Through calculations in specific embodiments, it is known that after replacing the stirring device, at least 11kw motor operation can be reduced, which can be converted into carbon emissions and can reduce carbon emissions by 0.785kg×11kw / h×24h×350d=72534kg / a=7.2534t / a. At the same time, after application, the utilization rate of Roots blower oxidation wind is increased from 64.32% to 91%, which not only reduces the problem of sulfur blocking and sulfur deposition, but also reduces the waste of wind energy, reduces costs and creates benefits, and is more conducive to environmental protection and sustainable development.
[0036] Unless otherwise defined, the technical terms or scientific terms used in this utility model shall have the usual meanings understood by people with ordinary skills in the field to which this utility model belongs. The terms "include" or "comprise" and similar words used in this utility model mean that the elements or objects appearing before the word include the elements or objects listed after the word and their equivalents, without excluding other elements or objects. "Connect" or "connected" and similar words are not limited to physical or mechanical connections, but may include electrical connections, whether direct or indirect.
[0037] At this point, those skilled in the art should recognize that, although the present invention has been described with reference to preferred embodiments, various modifications may be made thereto and components thereof may be replaced with equivalents without departing from the scope of the present invention. In particular, the various technical features mentioned in the various embodiments may be combined in any manner as long as there is no structural conflict. The present invention is not limited to the specific embodiments disclosed herein, but includes all technical solutions falling within the scope of the claims.
Claims
1. A desulfurization solution oxidation wind surplus recycling device, characterized in that: The invention comprises a Roots blower, wherein the vent of the Roots blower is connected with a main air pipe, the main air pipe is provided with a plurality of distribution pipes connected with the main air pipe, and the other ends of the distribution pipes are respectively provided with aeration pipes.
2. The desulfurization solution oxidation wind surplus recycling device according to claim 1 is characterized in that: The distribution pipe is provided with a regulating valve for adjusting the air intake volume of each level of the distribution pipe.
3. The desulfurization solution oxidation wind surplus recycling device according to claim 2 is characterized in that: The aeration pipe is a cross aeration pipe.
4. The desulfurization solution oxidation wind surplus recycling device according to claim 1 is characterized in that: The distribution pipe and the aeration pipe are located on the same center line.
5. The desulfurization solution oxidation wind surplus recycling device according to claim 1, characterized in that: The vent of the Roots blower is communicated with the main air pipe through a connecting flange.
6. The desulfurization solution oxidation wind surplus recycling device according to claim 2 is characterized in that: The aeration pipe is placed in the sulfur foam tank.
7. The desulfurization solution oxidation wind surplus recycling device according to claim 1 is characterized in that: The diameter of the main air pipe is DN40-DN60, the diameter of the distribution pipe is DN10-DN30, and the diameter of the aeration pipe is 8. The desulfurization solution oxidation wind surplus recycling device according to claim 1 is characterized in that: The distance between adjacent distribution pipes is 1.0 to 1.8 meters.
9. The desulfurization solution oxidation wind surplus recycling device according to claim 1, characterized in that: The distribution pipes are provided in 6 groups.
10. The desulfurization solution oxidation wind surplus recycling device according to claim 6, characterized in that: The regulating valve is arranged above the observation hole of the sulfur foam tank.