Compressed air purification device

By setting up an air-water separator, oil mist separator, fine dust collector and multi-stage filter, combined with differential pressure sensor monitoring, the problem of poor compressed air purification effect in the existing technology is solved, and an efficient and stable air purification effect is achieved.

CN223416912UActive Publication Date: 2025-10-10SHANGHAI MUFAN AUTOMOTIVE TECH CO LTD
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Patent Information

Application Number
CN202421855600.1
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-08-02
Publication Date
2025-10-10
Estimated Expiration
2034-08-02

AI Technical Summary

Technical Problem

Existing compressed air purification systems cannot meet the high quality requirements of modern industry and cannot effectively remove moisture, oil mist and tiny particles in the gas, resulting in poor purification effects.

Method used

An air-water separator, oil mist separator and fine dust collector are used for preliminary filtration, followed by a three-stage filter, including a slow-release pipeline and four purification branches. Each branch is equipped with a high-efficiency and ultra-high-efficiency filter, and is equipped with a differential pressure sensor to monitor the filter status, and finally collected into a BA-level gas storage tank.

Benefits of technology

It achieves efficient removal of moisture, oil mist and tiny particles, improves the purification quality of compressed air, reduces negative pressure loss, ensures stable purification effect and timely replacement of filters.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model belongs to the technical field of fluid, and discloses a compressed air purification device which comprises an air inlet end pipeline, a slow release pipeline, a collecting pipe and a purification pipeline which are sequentially arranged, and an air-water separator, an oil mist separator and a fine dust remover are sequentially arranged between the air inlet end pipeline and the slow release pipeline. The gas-water separator, the oil mist separator and the fine dust remover are arranged at the gas inlet end of the main pipeline, the gas enters the slow release pipeline after passing through the three-stage filter, the slow release pipeline is connected to the four purification branches, the efficient filter and the ultra-efficient filter are arranged on each purification branch, and finally the gas is collected to the BA-stage gas storage tank for downstream use. And purified compressed air can be provided.
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Description

Technical Field

[0001] The utility model relates to fluid technology, in particular to a compressed air purification device. Background Art

[0002] With the continuous development of industry, the quality requirements for compressed air are constantly increasing. Now most compressed air purification systems are still in the factory era and cannot meet new R&D and production needs. Utility Model Content

[0003] In response to the shortcomings of the existing technology, the utility model provides a compressed air purification device, which is equipped with an air-water separator, an oil mist separator, and a fine dust collector at the air inlet end of the main line. After passing through a three-stage filter, it enters a slow-release pipeline, which is connected to four purification branches. Each purification branch is equipped with a high-efficiency filter and an ultra-high-efficiency filter, and finally the air is collected in a BA-level air storage tank for downstream use, thereby providing purified compressed air.

[0004] In order to achieve the above purpose, the present invention adopts the following technical solutions:

[0005] A compressed air purification device comprises an air intake pipeline, a slow-release pipeline, a confluence pipe and a purification pipeline which are arranged in sequence; an air-water separator, an oil mist separator and a fine dust collector are arranged in sequence between the air intake pipeline and the slow-release pipeline.

[0006] As a further solution of the present invention, the diameter of the slow-release pipeline is twice the diameter of the air intake end pipeline.

[0007] As a further solution of the present invention, the diameter of the slow-release pipeline is 2 inches, and the diameter of the air inlet pipeline is 1 inch.

[0008] As a further solution of the present invention, the manifold includes a first manifold and a second manifold arranged in parallel.

[0009] As a further solution of the present invention, the purification pipeline includes four purification branches, the first manifold is connected to two purification branches, and the second manifold is connected to the other two purification branches, wherein the pipeline diameter of the purification branch is consistent with the diameter of the intake end pipeline.

[0010] As a further solution of the present invention, two high-efficiency filters and one ultra-high-efficiency filter are sequentially arranged on the purification branch, wherein the two high-efficiency filters are located between the manifold and the ultra-high-efficiency filter.

[0011] As a further solution of the present invention, the high efficiency filter and the ultra high efficiency filter are both provided with differential pressure sensors.

[0012] The utility model has the following beneficial effects:

[0013] The utility model discloses a main pipeline air inlet end is provided with gas -water separator, oil mist separator, fine dust collector, enters the slow -release pipeline after three -stage filter, and slow -release pipeline is connected to 4 purification branch, is provided with high -efficiency filter and super -high -efficiency filter on every purification branch, and finally gathers to BA grade gas holder for downstream use, can provide the compressed air after purification.

[0014] In order to more clearly set forth the structural features and efficacy of the utility model, the utility model will be described in detail below with the specific embodiments and the accompanying drawings. BRIEF DESCRIPTION OF DRAWINGS

[0015] Figure 1 It is the structure diagram of a compressed air purification device of the utility model. DETAILED DESCRIPTION

[0016] The utility model will be described further below with the accompanying drawings and relevant knowledge, and it is obviously that the application only is a part of the embodiment of the utility model, but not all the embodiment.

[0017] Referring to Figure 1 The utility model discloses a compressed air purification device, including air inlet end pipeline 1, slow -release pipeline 2, confluence pipe 3 and purification pipeline 4 that set gradually, air inlet end pipeline 1 with slow -release pipeline 2 between set gradually have gas -water separator 5, oil mist separator 6, fine dust collector 7. Through main pipeline air inlet end is provided with gas -water separator, oil mist separator, fine dust collector, enters slow -release pipeline after three -stage filter, and slow -release pipeline is connected to purification pipeline 4, finally gathers to BA grade gas holder for downstream use, can provide the compressed air after purification. In the utility model, slow -release pipeline is convenient for the slow passage of gas, and subsequent filtration is facilitated, and further gas is shunted by setting the confluence pipe, better purification is realized, and more specifically, the use of the confluence pipe not only effectively reduces the negative pressure loss, increases the single-channel negative pressure, and effectively improves the pumping negative pressure.

[0018] In the utility model, the diameter of slow -release pipeline 2 is 2 times of the diameter of air inlet end pipeline 1, and further preferably, the diameter of slow -release pipeline is 2 inches, and the diameter of air inlet end pipeline is 1 inch, so that the pressure at the air inlet end is greater than the pressure of slow -release pipeline, the air inlet is facilitated into the purification device, and subsequent purification of the gas is facilitated, and the processing flow can be realized: 10bar pressure, maximum flow 3000SLPM.

[0019] In the utility model, the confluence pipe 3 includes the first confluence pipe and the second confluence pipe arranged side by side, so that the compressed air can enter the slow -release pipeline after three -stage filtration, and then be shunted by the confluence pipe.

[0020] Furthermore, the purification pipeline 4 includes four purification branches. The first confluence pipe is connected to two purification branches, and the second confluence pipe is connected to the other two purification branches. That is to say, after passing through the confluence pipe, it branches into four purification branches, which can carry out subsequent purification more efficiently.

[0021] As a further solution of the present invention, two high-efficiency filters 8 and an ultra-high-efficiency filter 9 are sequentially installed on the purification branch, wherein the two high-efficiency filters are located between the manifold and the ultra-high-efficiency filter. It is further preferred that both the high-efficiency filter and the ultra-high-efficiency filter are equipped with differential pressure sensors. After the compressed air passes through the three-stage filtration, it enters the slow-release pipeline, which is connected to four purification branches. Each purification branch first passes through two high-efficiency filters, and then an ultra-high-efficiency filter is connected to the rear end of the high-efficiency filter. Each filter is equipped with a differential pressure sensor to monitor the change from initial pressure to final resistance pressure. When the final resistance pressure is reached, an alarm message is output to remind the replacement of the filter element.

[0022] To sum up, the air inlet end pipeline of the utility model is a 1-inch compression fitting, which is connected to the gas-water separator, oil mist separator, fine dust collector, and connected to a 1-inch to 2-inch VCR adapter. The adapter is connected to a 2-inch slow-release pipeline, and the slow-release pipeline is connected to the manifold. The three 1-inch connectors of the manifold are connected to four purification branches. A pressure difference is formed between the air inlet end and the air outlet end to facilitate the passage of gas. Preferably, the diameter of the slow-release pipeline is twice the diameter of the air inlet end, and the pipeline diameter of the purification branch is consistent with the diameter of the air inlet end pipeline. The above-mentioned pipeline can realize convenient entry and passage of gas and can achieve better subsequent filtration effect, mainly through the manifold and then through the purification branch to achieve better filtration. That is to say, by setting four purification branches, it is convenient to achieve better purification effect. Each purification branch first passes through two high-efficiency filters, and the rear end of the high filter is connected to an ultra-high-efficiency filter, and finally reaches the BA-level gas storage tank. Each filter is equipped with a differential pressure sensor to monitor the change from initial pressure to final resistance pressure. When the final resistance pressure is reached, an alarm message is output to remind you to replace the filter element.

[0023] The technical principles of the present invention have been described above in conjunction with specific embodiments, which are only preferred embodiments of the present invention. It should be understood that although this specification describes the embodiments, not each embodiment contains only one independent technical solution. This description is only for the sake of clarity. Those skilled in the art should regard the specification as a whole. The technical solutions in the various embodiments can also be appropriately combined to form other embodiments that can be understood by those skilled in the art, all of which fall within the scope of protection of the present invention.

Claims

1. A compressed air purification device, characterized in that: The invention comprises an air intake pipeline, a slow-release pipeline, a confluence pipe and a purification pipeline which are arranged in sequence. An air-water separator, an oil mist separator and a fine dust collector are arranged in sequence between the air intake pipeline and the slow-release pipeline.

2. A compressed air purification device according to claim 1, characterized in that: The diameter of the slow-release pipeline is twice the diameter of the air inlet pipeline.

3. A compressed air purification device according to claim 1, characterized in that: The diameter of the slow-release pipe is 2 inches, and the diameter of the air inlet pipe is 1 inch.

4. A compressed air purification device according to claim 1, characterized in that: The manifold includes a first manifold and a second manifold arranged in parallel.

5. A compressed air purification device according to claim 4, characterized in that: The purification pipeline includes four purification branches, the first manifold is connected to two purification branches, and the second manifold is connected to the other two purification branches, wherein the pipeline diameter of the purification branch is consistent with the diameter of the intake end pipeline.

6. A compressed air purification device according to claim 5, characterized in that: Two high efficiency filters and one ultra high efficiency filter are sequentially arranged on the purification branch, wherein the two high efficiency filters are located between the manifold and the ultra high efficiency filter.

7. A compressed air purification device according to claim 6, characterized in that: The high efficiency filter and the ultra high efficiency filter are both provided with a differential pressure sensor.