Device for testing adsorption performance of zeolite molecular sieve

By designing a device for testing the adsorption performance of zeolite molecular sieve, the problem of poor adsorption performance of zeolite molecular sieve in the tire rubber industry is solved, the raw material ratio is optimized, and the adsorption performance and practicality of zeolite molecular sieve is improved.

CN222529205UActive Publication Date: 2025-02-25DEZHOU GUANGYUAN ENVIRONMENTAL PROTECTION TECH
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Patent Information

Application Number
CN202422824031.0
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-11-20
Publication Date
2025-02-25
Estimated Expiration
2034-11-20

AI Technical Summary

Technical Problem

The lack of optimization of raw material ratio of zeolite molecular sieve for the tire rubber industry in the prior art has led to poor adsorption performance of zeolite molecular sieve in adsorbing different VOCS gases.

Method used

Design a device to test the adsorption performance of zeolite molecular sieve, including a three-stage filter box, a zeolite adsorption box, a high-pressure blower and a detection tube. The exhaust gas is filtered and adsorbed, and the particulate matter and exhaust gases are detected in real time, and the waste gases of different ingredients are analyzed for zeolites. Effects of adsorption properties of molecular sieve.

Benefits of technology

Through the online data analysis of the device, the raw material ratio of zeolite molecular sieve can be optimized and its performance in adsorbing different VOCS gases can be improved, thereby producing zeolite molecular sieves that are relatively to the tire rubber industry, improving practicality.

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Abstract

The utility model relates to the technical field of zeolite molecular sieves, and discloses a device for testing the adsorption performance of a zeolite molecular sieve, which comprises a support frame, the left part of the upper end of the support frame is fixedly connected with two support seats, and the upper ends of the two support seats are jointly and fixedly connected with a three-stage filter box in a penetrating manner; a waste gas inlet pipe is fixedly connected to the middle of the left end of the third-stage filter box in a penetrating mode, a waste gas conveying pipe is fixedly connected to the middle of the right end of the third-stage filter box in a penetrating mode, and a zeolite adsorption box is fixedly connected to the end, away from the third-stage filter box, of the waste gas conveying pipe in a penetrating mode; a high-pressure blower is fixedly connected to the middle of the lower end of the zeolite adsorption box in a penetrating manner, and a waste gas outlet pipe is fixedly connected to one end, away from the zeolite adsorption box, of the high-pressure blower in a penetrating manner. The device for testing the adsorption performance of the zeolite molecular sieve can solve the problem of the adsorption performance of the zeolite molecular sieve in adsorption of different VOCS gases, so that the ratio of raw materials of the zeolite molecular sieve is optimized, and the device is suitable for being widely used.
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Description

Technical Field

[0001] The utility model relates to the technical field of zeolite molecular sieves, in particular to a device for testing the adsorption performance of zeolite molecular sieves. Background Art

[0002] Zeolite molecular sieve is a hydrate of crystalline aluminum silicate metal salt. It has the structure and characteristics of crystals, with a solid skeleton on the surface. The internal holes can play the role of adsorbing molecules. The holes are connected by channels, and the molecules pass through the channels. Due to the clean nature of the holes, the pore size distribution of the molecular sieve is very uniform. The molecular sieve selectively adsorbs molecules according to the size of the holes inside its crystal, that is, it adsorbs molecules of a certain size and excludes molecules of larger substances. Zeolite molecular sieve is a selective adsorption material, and its adsorption performance for different exhaust gases is different. When zeolite molecular sieve is mainly used in the tire rubber industry, due to the complex composition of the exhaust gas in the tire rubber industry and the different exhaust gas components produced by different ingredients, and there is no relative zeolite molecular sieve produced for the tire rubber industry on the market, it is necessary to optimize the ratio of the raw materials of the zeolite molecular sieve to solve the adsorption performance of the zeolite molecular sieve in the adsorption of different VOCS gases. Therefore, we have introduced a device to test the adsorption performance of zeolite molecular sieve. Utility Model Content

[0003] The main purpose of the utility model is to provide a device for testing the adsorption performance of zeolite molecular sieves, which can effectively solve the problems in the background technology.

[0004] In order to achieve the above purpose, the technical solution adopted by the utility model is:

[0005] A device for testing the adsorption performance of zeolite molecular sieve, comprising a support frame, wherein the left portion of the upper end of the support frame is fixedly connected to two support seats, a three-stage filter box is interspersed and fixedly connected between the upper ends of the two support seats, an exhaust gas inlet pipe is interspersed and fixedly connected to the middle portion of the left end of the three-stage filter box, an exhaust gas transmission pipe is interspersed and fixedly connected to the middle portion of the right end of the three-stage filter box, a zeolite adsorption box is interspersed and fixedly connected to the end of the exhaust gas transmission pipe away from the three-stage filter box, a high-pressure blower is interspersed and fixedly connected to the middle portion of the lower end of the zeolite adsorption box, and an exhaust gas outlet pipe is interspersed and fixedly connected to the end of the high-pressure blower away from the zeolite adsorption box.

[0006] Preferably, the zeolite adsorption box includes an adsorption box body, the left box wall and the right box wall of the adsorption box body are fixedly connected to a plurality of fixing frames, and a storage frame is commonly clamped between the corresponding fixing frames on the left and right sides, and a plurality of zeolite molecular sieve bodies are placed inside the plurality of storage frames, and the upper and lower ends of the adsorption box body are respectively fixedly connected to the exhaust gas transmission pipe and the high-pressure blower through the insertion.

[0007] Preferably, several of the fixing frames are configured as L-shaped structures, several ventilation holes are opened on the lower frame walls of several of the storage frames, and the zeolite adsorption box and the three-stage filter box are configured as airtight and airtight structures.

[0008] Preferably, a particle detection tube and an exhaust gas detection tube are inserted and fixedly connected on the upper portion of the outer surface of the exhaust gas transmission pipe, and the particle detection tube is located above the exhaust gas detection tube.

[0009] Preferably, a drying box is installed in the middle of the upper end of the three-stage filter box, an outer shell is fixedly connected between the upper end periphery of the support frame, an electric control box is fixedly connected to the front right part of the outer shell, two box doors are provided in the middle of the front shell wall of the outer shell, and the left shell wall and the right shell wall of the outer shell are respectively fixedly connected with the left end of the exhaust gas inlet pipe and the right end of the exhaust gas outlet pipe.

[0010] Preferably, the electric control box is electrically connected to the drying box, the high-pressure blower and the three-stage filter box, the right end of the particle detection tube is connected to a particle detector, and the right end of the exhaust gas detection tube is connected to a portable PID.

[0011] Compared with the prior art, the utility model has the following beneficial effects:

[0012] During the use of the device for testing the adsorption performance of zeolite molecular sieves of the utility model, the exhaust gas is filtered through a three-stage filter box to make the particulate matter therein less than 1 mg / m³, and then the filtered exhaust gas is sucked into the zeolite adsorption box by the suction force of a high-pressure blower, and the exhaust gas is adsorbed by a plurality of zeolite molecular sieves in the zeolite adsorption box, and finally two particulate matter detectors and two portable PIDs are used to detect the particulate matter and exhaust gas in the particulate matter detection tube and the exhaust gas detection tube, respectively, and the particulate matter and exhaust gas in the exhaust gas outlet pipe are detected at the same time, so as to form an online data analysis of the influence of exhaust gas with different ingredients on the adsorption performance of the zeolite molecular sieve, so that the device can solve the adsorption performance problem of the zeolite molecular sieve in the adsorption of different VOCS gases, thereby optimizing the ratio of the raw materials of the zeolite molecular sieve, and producing zeolite molecular sieves relative to the tire rubber industry, thereby improving practicality. BRIEF DESCRIPTION OF THE DRAWINGS

[0013] Figure 1 This is a schematic diagram of the overall structure of a device for testing the adsorption performance of zeolite molecular sieves according to the utility model;

[0014] Figure 2 This is a schematic diagram of the overall internal structure of a device for testing the adsorption performance of zeolite molecular sieves according to the utility model;

[0015] Figure 3 This is a schematic diagram of the overall structure of a zeolite adsorption box of a device for testing the adsorption performance of zeolite molecular sieves according to the utility model;

[0016] Figure 4 The utility model is a schematic diagram of the overall structure of the shell of a device for testing the adsorption performance of zeolite molecular sieves.

[0017] In the figure: 1. support frame; 2. support base; 3. three-stage filter box; 4. exhaust gas inlet pipe; 5. exhaust gas transmission pipe; 6. zeolite adsorption box; 7. high-pressure blower; 8. exhaust gas outlet pipe; 9. drying box; 10. outer shell; 11. electric control box; 12. box door; 51. particle detection tube; 52. exhaust gas detection tube; 61. adsorption box; 62. fixing frame; 63. storage frame; 64. zeolite molecular sieve body. DETAILED DESCRIPTION

[0018] In order to make the technical means, creative features, objectives and effects achieved by the present invention easy to understand, the present invention is further described below in conjunction with specific implementation methods.

[0019] In the description of the present invention, it should be noted that the terms "upper", "lower", "inner", "outer", "front end", "rear end", "two ends", "one end", "the other end" and the like indicate positions or positional relationships based on the positions or positional relationships shown in the drawings, and are only for the convenience of describing the present invention and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operate in a specific orientation, and therefore cannot be understood as a limitation on the present invention. In addition, the terms "first" and "second" are used for descriptive purposes only and cannot be understood as indicating or implying relative importance.

[0020] In the description of the present invention, it should be noted that, unless otherwise clearly specified and limited, the terms "installed", "provided with", "connected", etc. should be understood in a broad sense. For example, "connected" can be a fixed connection, a detachable connection, or an integral connection; it can be a mechanical connection or an electrical connection; it can be a direct connection, or it can be an indirect connection through an intermediate medium, or it can be the internal communication of two components. For ordinary technicians in this field, the specific meanings of the above terms in the present invention can be understood according to specific circumstances.

[0021] See also Figure 1-4 , the utility model provides a technical solution:

[0022] A device for testing the adsorption performance of zeolite molecular sieves, comprising a support frame 1, two support seats 2 are fixedly connected to the left upper end of the support frame 1, a three-stage filter box 3 is interspersed and fixedly connected between the upper ends of the two support seats 2, an exhaust gas inlet pipe 4 is interspersed and fixedly connected to the middle of the left end of the three-stage filter box 3, an exhaust gas transmission pipe 5 is interspersed and fixedly connected to the middle of the right end of the three-stage filter box 3, a zeolite adsorption box 6 is interspersed and fixedly connected to the end of the exhaust gas transmission pipe 5 away from the three-stage filter box 3, a high-pressure blower 7 is interspersed and fixedly connected to the middle of the lower end of the zeolite adsorption box 6, and an exhaust gas outlet pipe 8 is interspersed and fixedly connected to the end of the high-pressure blower 7 away from the zeolite adsorption box 6.

[0023] In this embodiment, the zeolite adsorption box 6 includes an adsorption box body 61, and the left box wall and the right box wall of the adsorption box body 61 are fixedly connected with a plurality of fixing frames 62, and a storage frame 63 is commonly clamped between the corresponding plurality of fixing frames 62 on the left and right sides, and a plurality of zeolite molecular sieve bodies 64 are placed inside the plurality of storage frames 63. The upper and lower ends of the adsorption box body 61 are respectively interlaced and fixedly connected with the exhaust gas transmission pipe 5 and the high-pressure blower 7; the plurality of fixing frames 62 are all set to an L-shaped structure, so that the fixing frames 62 limit and fix the storage frame 63 stably, and the lower frame walls of the plurality of storage frames 63 are provided with a plurality of ventilation holes, so that the exhaust gas can pass through the storage frame 63 and enter the zeolite molecular sieve body 64 of the storage frame 63 below it for adsorption. The zeolite adsorption box 6 and the three-stage filter box 3 are both set to a closed and airtight structure, which can ensure that no outside air enters the zeolite adsorption box 6 and the three-stage filter box 3 to dilute the exhaust gas therein.

[0024] In this embodiment, a particle detection tube 51 and an exhaust gas detection tube 52 are interspersed and fixedly connected on the upper part of the outer surface of the exhaust gas transmission pipe 5, and the particle detection tube 51 is located above the exhaust gas detection tube 52; a drying box 9 is installed in the middle of the upper end of the three-stage filter box 3, and a shell 10 is fixedly connected between the upper end periphery of the support frame 1, and an electric control box 11 is fixedly connected to the front right part of the shell 10, and two box doors 12 are arranged in the middle of the front shell wall of the shell 10, and the left shell wall and the right shell wall of the shell 10 are respectively interspersed and fixedly connected with the left end of the exhaust gas inlet pipe 4 and the right end of the exhaust gas outlet pipe 8; the electric control box 11 is electrically connected to the drying box 9, the high-pressure blower 7 and the three-stage filter box 3, and PLC control can be used to accurately control the device, the right end of the particle detection tube 51 is connected to the particle detector, and the right end of the exhaust gas detection tube 52 is connected to the portable PID to realize the classification detection of the exhaust gas.

[0025] It should be noted that the utility model is a device for testing the adsorption performance of zeolite molecular sieves. During use, a hole is firstly opened on the main pipeline for collecting exhaust gas, and the exhaust gas intake pipe 4 is connected to the main pipeline through the hole, so that the exhaust gas enters the third-stage filter box 3 through the exhaust gas intake pipe 4 for filtration, so that the particulate matter in the exhaust gas is less than 1 mg / m³, and then the high-pressure blower 7 is used to generate suction, so that the exhaust gas transmission pipe 5 sucks the filtered exhaust gas into the adsorption box 61, and the exhaust gas is adsorbed by a plurality of zeolite molecular sieve bodies 64 in a plurality of storage frames 63, and finally the exhaust gas after adsorption treatment is discharged through the exhaust gas outlet pipe 8, and in the process of filtering and adsorbing the exhaust gas by the device, the particulate matter connected to the particle detection tube 51 is The particle detector and the portable PID connected to the exhaust gas detection tube 52 can respectively detect the particulate matter and exhaust gas in the particle detection tube 51 and the exhaust gas detection tube 52, and then the particle detector and the portable PID connected to the particle detection tube 51 can simultaneously detect the particulate matter and exhaust gas in the exhaust gas outlet pipe 8, thereby forming an online data analysis of the influence of exhaust gases with different ingredients on the adsorption performance of the zeolite molecular sieve, and then the drying box 9 is used for drying and desorption, and the repeated adsorption is analyzed to analyze the repeated adsorption performance of the zeolite molecular sieve, so that the device can solve the adsorption performance problem of the zeolite molecular sieve in the adsorption of different VOCS gases, thereby optimizing the ratio of the raw materials of the zeolite molecular sieve, and can produce zeolite molecular sieves that are relatively comparable to the tire rubber industry, thereby improving practicality.

[0026] The above shows and describes the basic principle and main features of the utility model and the advantages of the utility model. Those skilled in the art should understand that the utility model is not limited by the above embodiments. The above embodiments and descriptions are only for explaining the principle of the utility model. Without departing from the spirit and scope of the utility model, the utility model may have various changes and improvements, which fall within the scope of the utility model to be protected. The scope of protection claimed by the utility model is defined by the attached claims and their equivalents.

Claims

1. A device for testing the adsorption performance of a zeolite molecular sieve, comprising a support frame (1), characterized in that: Two support seats (2) are fixedly connected to the left upper end of the support frame (1); a three-stage filter box (3) is interspersed and fixedly connected between the upper ends of the two support seats (2); an exhaust gas inlet pipe (4) is interspersed and fixedly connected to the middle of the left end of the three-stage filter box (3); an exhaust gas transmission pipe (5) is interspersed and fixedly connected to the middle of the right end of the three-stage filter box (3); a zeolite adsorption box (6) is interspersed and fixedly connected to the end of the exhaust gas transmission pipe (5) away from the three-stage filter box (3); a high-pressure blower (7) is interspersed and fixedly connected to the middle of the lower end of the zeolite adsorption box (6); and an exhaust gas outlet pipe (8) is interspersed and fixedly connected to the end of the high-pressure blower (7) away from the zeolite adsorption box (6); The zeolite adsorption box (6) comprises an adsorption box body (61), the left box wall and the right box wall of the adsorption box body (61) are fixedly connected to a plurality of fixing frames (62), and a storage frame (63) is commonly clamped between the corresponding fixing frames (62) on the left and right sides, and a plurality of zeolite molecular sieve bodies (64) are placed inside the plurality of storage frames (63). The upper end and the lower end of the adsorption box body (61) are respectively interlaced and fixedly connected to the exhaust gas transmission pipe (5) and the high-pressure blower (7).

2. A device for testing the adsorption performance of zeolite molecular sieve according to claim 1, characterized in that: The plurality of fixing frames (62) are each configured as an L-shaped structure, the lower frame walls of the plurality of storage frames (63) are each provided with a plurality of ventilation holes, and the zeolite adsorption box (6) and the third-stage filter box (3) are each configured as a sealed, airtight structure.

3. A device for testing the adsorption performance of zeolite molecular sieve according to claim 2, characterized in that: A particle detection tube (51) and an exhaust gas detection tube (52) are inserted and fixedly connected on the upper portion of the outer surface of the exhaust gas transmission tube (5), and the particle detection tube (51) is located above the exhaust gas detection tube (52).

4. A device for testing the adsorption performance of zeolite molecular sieve according to claim 3, characterized in that: A drying box (9) is installed in the middle of the upper end of the three-stage filter box (3), a shell (10) is fixedly connected between the upper end periphery of the support frame (1), an electric control box (11) is fixedly connected to the front right part of the shell (10), two box doors (12) are arranged in the middle of the front shell wall of the shell (10), and the left shell wall and the right shell wall of the shell (10) are respectively inserted and fixedly connected to the left end of the exhaust gas inlet pipe (4) and the right end of the exhaust gas outlet pipe (8).

5. A device for testing the adsorption performance of zeolite molecular sieve according to claim 4, characterized in that: The electric control box (11) is electrically connected to the drying box (9), the high-pressure blower (7) and the three-stage filter box (3); the right end of the particle detection tube (51) is connected to a particle detector; and the right end of the exhaust gas detection tube (52) is connected to a portable PID.

Citation Information

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