Novel zero-gas-consumption adsorption type dryer

Abstract

The invention provides a novel zero-gas-consumption adsorption type dryer which comprises a supporting base, two drying towers, a storage tank and an air pump set, the two drying towers are arranged on one side of the supporting base, the positions of the drying towers on the two sides are symmetrically arranged, the storage tank is arranged on the other side of a heating plate, the top ends of the drying towers are communicated with product air pipes, and the product air pipes are communicated with the air pump set. And a pipeline switching valve is arranged between the openings of the product air pipes on the two sides in a communicating manner. Product gas is input into the backflow pipeline through the communicated communicating pipeline, the final product gas flows into the tail end in the spiral pipeline, circulation of the product gas is achieved, heat exchange work is conducted on the heating plate and the interior of the drying cavity through the product gas, cooling of the interior of the drying cavity is promoted, and the drying efficiency is improved. The internal cooling of the drying tower is further facilitated, the subsequent drying work is facilitated, zero gas consumption is realized, and the energy consumption is further reduced.

Description

Technical Field

[0001] The invention relates to the technical field of air separation processing, in particular to a novel zero-gas-consumption adsorption dryer. Background Art

[0002] In the existing air separation processing technology, the treatment and drying of compressed air is a key link. Traditional drying equipment usually requires external energy to heat the regeneration air during the regeneration process, which not only increases energy consumption but also limits the overall energy efficiency of the equipment. In addition, traditional equipment often generates large pneumatic power losses during the adsorption and regeneration process, further affecting the economy and environmental protection of the equipment.

[0003] However, when utilizing waste heat resources, some equipment fails to fully utilize the high-temperature compressed air discharged by the air compressor, resulting in low regeneration efficiency. Summary of the invention

[0004] 1. Technical issues to be solved

[0005] In view of the deficiencies of the prior art, the present invention provides a novel zero-gas consumption adsorption dryer, which solves the problems raised in the above-mentioned background technology.

[0006] (II) Technical solution

[0007] To achieve the above objectives, the present invention is implemented through the following technical solutions: a new type of zero-gas consumption adsorption dryer, comprising a supporting base, two drying towers, a storage tank and an air pump group, the two drying towers are set on one side of the supporting base, the drying towers on both sides are symmetrically arranged, the storage tank is set on the other side of the heating plate, the top of the drying tower is connected with a product air pipe, the openings of the product air pipes on both sides are connected with a pipeline switching valve, the top of the storage tank is connected with a product storage pipe, one end face of the product storage pipe is connected with the side face of the pipeline switching valve, a switch is provided at the top of the pipeline switching valve, the other side of the outer end face of the pipeline switching valve is connected with a connecting pipe, the air pump group is set between the drying tower and the storage tank, and one side of the outer end face of the storage tank is connected with a product output pipe.

[0008] Preferably, a drying chamber is provided in the drying towers on both sides, the drying chamber is trapezoidal, a plurality of molecular plates arranged in an array from top to bottom are provided in the drying chamber, and open and connected air flow holes are provided on the inner circumference of the molecular plates.

[0009] Furthermore, a heating plate is fixedly provided on the outer end surface of the drying tower, a spiral pipe with an annular thread shape is provided inside the heating plate, an output pipe is connected to the top end of the spiral pipe, the tail ends of the output pipes on both sides are connected to the same return pipe, and the middle position of the return pipe is connected to the connecting pipe.

[0010] Preferably, the output pipes on both sides are connected to the air inlet pipe at the bottom of the storage tank.

[0011] Preferably, a heating plate is provided inside the heating plate, and the heating plate can heat the interior of the drying chamber.

[0012] Preferably, an exhaust hole is provided on the upper side of the outer end surface of the drying tower, the exhaust hole is connected to the inner wall of the drying chamber, and an on-off valve is provided in the exhaust hole.

[0013] Preferably, an air flow detector is provided at the top of the drying tower, and the air flow detector can detect the flow rate of the gas flowing through the product air pipe.

[0014] Preferably, a flow diverter is connected to the front end of the air pump group, and two flow diverter pipes are connected to the end surfaces on both sides of the flow diverter.

[0015] Preferably, stabilizing brackets are fixedly provided at both ends of the support base, and the stabilizing brackets on both sides are symmetrically arranged. An input pipe opening is connected to the bottom of the drying tower, and the input pipe opening passes through the stabilizing bracket, and the stabilizing bracket plays a role of stabilizing support.

[0016] Preferably, the input pipe opening is connected to the diversion pipe via a connecting pipe.

[0017] (III) Beneficial effects

[0018] The present invention provides a novel zero-gas consumption adsorption dryer, which has the following beneficial effects:

[0019] 1. The present invention adsorbs wet air through the array of molecular plates, and guides the trapezoidal drying chamber to gradually enrich and output the wet air upward, adsorbs moisture on the wet air multiple times, and finally outputs the dry gas product through the product gas pipe to the pipeline switching valve, and inputs it into the connected product storage pipe, and then inputs the dry gas product into the storage tank for storage.

[0020] 2. The present invention inputs the product gas into the reflux pipe through the connected connecting pipe, and finally the product gas flows into the tail end of the spiral pipe to realize the circulation of the product gas, and the product gas performs heat exchange on the heating plate and the inside of the drying chamber, thereby promoting the cooling of the inside of the drying chamber, and further facilitating the internal cooling of the drying tower, facilitating subsequent drying work, achieving zero gas consumption, and further reducing energy consumption. BRIEF DESCRIPTION OF THE DRAWINGS

[0021] Figure 1 It is a schematic diagram of the appearance structure of the present invention;

[0022] Figure 2This is a front view of the appearance structure of the present invention;

[0023] Figure 3 This is a perspective view of the appearance structure of the present invention;

[0024] Figure 4 It is a front view of the appearance structure of the present invention;

[0025] Figure 5 A top view of the appearance structure of the present invention;

[0026] Figure 6 For the present invention Figure 5 Cross-sectional view along the AA direction.

[0027] In the figure: 101, support base; 102, return pipe; 103, spiral pipe; 104, input pipe mouth; 105, stable bracket; 106, heating plate; 107, connecting pipe; 108, exhaust hole; 109, on-off valve; 110, output pipe; 111, drying tower; 112, air flow detector; 113, product air pipe; 114, pipeline switching valve; 115, switch; 116, product storage pipe; 117, storage tank; 118, air pump group; 119, diverter; 120, diverter pipe; 121, product output pipe; 122, drying chamber; 123, air flow hole; 124, molecular plate. DETAILED DESCRIPTION

[0028] The embodiment of the present invention provides a novel zero-gas consumption adsorption dryer, such as Figure 1-6 As shown, it includes a supporting base 101, two drying towers 111, a storage tank 117 and an air pump group 118. The two drying towers 111 are set up on one side of the supporting base 101, and the drying towers 111 on both sides are symmetrically arranged. The storage tank 117 is set up on the other side of the heating plate 106. The top of the drying tower 111 is connected with a product air pipe 113, and the openings of the product air pipes 113 on both sides are connected with a pipeline switching valve 114. The top of the storage tank 117 is connected with a product storage pipe 116. One end face of the product storage pipe 116 is connected to the side face of the pipeline switching valve 114. A switcher 115 is provided on the top of the pipeline switching valve 114. The other side of the outer end face of the pipeline switching valve 114 is connected with a connecting pipe 107. The air pump group 118 is set up between the drying tower 111 and the storage tank 117, and one side of the outer end face of the storage tank 117 is connected with a product output pipe 121.

[0029] It should be further explained that the switch 115 can adjust the connectivity between the product gas pipes 113, the product storage pipe 116 and the connecting pipe 107 on both sides by rotating.

[0030] Furthermore, a drying chamber 122 is provided in the drying towers 111 on both sides. The drying chamber 122 is trapezoidal and has a plurality of molecular plates 124 arranged in an array from top to bottom. The inner circumference of the molecular plates 124 is provided with open and connected air flow holes 123 .

[0031] It should be further explained that the molecular plate 124 is filled with a high-efficiency adsorbent, which can adsorb the moisture in the input humid air to achieve the effect of drying the air.

[0032] Furthermore, a heating plate 106 is fixedly provided on the outer end surface of the drying tower 111, and a spiral pipe 103 with an annular thread shape is provided inside the heating plate 106. The top end of the spiral pipe 103 is connected to an output pipe 110, and the tail ends of the output pipes 110 on both sides are connected to the same return pipe 102, and the middle position of the return pipe 102 is connected to the connecting pipe 107.

[0033] Furthermore, the output pipes 110 on both sides are connected to the air intake pipe at the bottom of the storage tank 117 .

[0034] Furthermore, a heating plate is provided inside the heating plate 106 , and the heating plate 106 can heat the interior of the drying chamber 122 .

[0035] It should be further explained that the connection position between the heating plate 106 and the drying tower 111 is made of heat exchange material.

[0036] Furthermore, an exhaust hole 108 is provided on the upper side of the outer end surface of the drying tower 111 , and the exhaust hole 108 is connected to the inner wall of the drying chamber 122 . An on-off valve 109 is provided in the exhaust hole 108 .

[0037] It is worth further explaining that the rotating on-off valve 109 can control the on-off status of the exhaust hole 108 .

[0038] Furthermore, an airflow detector 112 is provided at the top of the drying tower 111 , and the airflow detector 112 can detect the flow rate of the gas flowing through the product gas pipe 113 .

[0039] Furthermore, a flow divider 119 is connected to the front end of the air pump assembly 118 , and two flow divider pipes 120 are connected to the end surfaces on both sides of the flow divider 119 .

[0040] Furthermore, stabilizing brackets 105 are fixedly provided at both ends of the support base 101, and the stabilizing brackets 105 on both sides are symmetrically arranged. An input pipe port 104 is connected to the bottom of the drying tower 111, and the input pipe port 104 passes through the stabilizing bracket 105, and the stabilizing bracket 105 plays a role of stabilizing support.

[0041] Furthermore, the input pipe opening 104 is connected to the flow diversion pipe 120 via a connecting pipe.

[0042] It should be further explained that the inlet of the air pump assembly 118 is connected to the output pipe opening of the wet air tank to be dried.

[0043] When using this solution, first start the air pump group 118 and draw the wet air in the wet air tank into the wet air tank and divert it through the diverter 119, and then output the wet air to the connected input pipe port 104 through the diversion pipe 120, and input the wet air into the drying chamber 122 in the drying tower 111 through the input pipe port 104. As the wet air flows from bottom to top, the wet air is adsorbed by the array molecular plates 124, and guided by the trapezoidal drying chamber 122, the wet air is gradually enriched upward. During the output process, the wet air is subjected to multiple moisture adsorption, and finally the dry gas product is output to the outside through the product gas pipe 113 to the pipeline switching valve 114, and input into the connected product storage pipe 116, and the dry gas product is input into the storage tank 117 for storage.

[0044] After the drying towers 111 on both sides have been working for a period of time, the internal molecular plate 124 has absorbed a lot of water. The staff turns the switch 115 on the top. At this time, the pipeline switching valves 114 on both sides are disconnected, and the product storage pipe 116 is connected to the connecting pipe 107. At the same time, the staff opens the on-off valve 109 and connects the exhaust hole 108 to the outside. At this time, the heating plate 106 is started in the heating plate 106, and the heating plate 106 can heat the inside of the drying chamber 122. At this time, as the inside of the drying chamber 122 is heated, the water molecules in the adsorption material in the molecular plate 124 evaporate and are output to the outside through the exhaust hole 108 with the air flow. After a period of adsorbent regeneration work, as the heating plate 106 and the surface of the drying tower 111 are attached to the temperature inside the drying chamber 122 for heat exchange, the heating plate 1 06 is exchanged to the spiral pipe 103. At this time, the air in the spiral pipe 103 heats up and expands, and the air is promoted to flow into the storage tank 117 through the output pipe 110. At this time, the product gas in the storage tank 117 is input upward into the product storage pipe 116 due to the air flow, and is input into the pipeline switching valve 114 through the product storage pipe 116, and is input into the return pipe 102 through the connected connecting pipe 107, and finally the product gas flows into the tail end of the spiral pipe 103, so as to realize the circulation of the product gas, and the product gas is used to perform heat exchange with the heating plate 106 and the inside of the drying chamber 122, so as to promote the cooling of the inside of the drying chamber 122, and further facilitate the internal cooling of the drying tower 111, so as to facilitate the subsequent drying work, realize zero gas consumption, and further reduce energy consumption.

[0045] Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and variations may be made to the embodiments without departing from the principles and spirit of the present invention, and that the scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. A novel zero-gas consumption adsorption dryer, comprising a support base (101), two drying towers (111), a storage tank (117) and an air pump group (118), characterized in that: The two drying towers (111) are set up on one side of the support base (101), and the drying towers (111) on both sides are symmetrically arranged. The storage tank (117) is set up on the other side of the heating plate (106). The top of the drying tower (111) is connected to a product gas pipe (113), and the openings of the product gas pipes (113) on both sides are connected to a pipeline switching valve (114). The top of the storage tank (117) is connected to a product storage pipe (116), and one end surface of the product storage pipe (116) is connected to the side surface of the pipeline switching valve (114). The top of the pipeline switching valve (114) is provided with a switch (115), and the other side of the outer end surface of the pipeline switching valve (114) is connected to a connecting pipe (107). The air pump group (118) is set up between the drying tower (111) and the storage tank (117), and one side of the outer end surface of the storage tank (117) is connected to a product output pipe (121).

2. A novel zero-gas consumption adsorption dryer according to claim 1, characterized in that: The drying towers (111) on both sides are provided with drying chambers (122), and a plurality of molecular plates (124) arranged in an array from top to bottom are provided in the drying chambers (122), and open and connected air flow holes (123) are provided on the inner circumference of the molecular plates (124).

3. A novel zero-gas consumption adsorption dryer according to claim 1, characterized in that: A heating plate (106) is fixedly provided on the outer end surface of the drying tower (111), a spiral pipe (103) with an annular thread shape is provided inside the heating plate (106), an output pipe (110) is connected to the top end of the spiral pipe (103), the tail ends of the output pipes (110) on both sides are connected to the same return pipe (102), and the middle position of the return pipe (102) is connected to the connecting pipe (107).

4. A novel zero-gas consumption adsorption dryer according to claim 3, characterized in that: The output pipes (110) on both sides are connected to the air intake pipe at the bottom of the storage tank (117).

5. A novel zero-gas consumption adsorption dryer according to claim 4, characterized in that: A heating plate is provided inside the heating plate (106), and the heating plate (106) is capable of heating the interior of the drying chamber (122).

6. A novel zero-gas consumption adsorption dryer according to claim 1, characterized in that: An exhaust hole (108) is provided on the upper side of the outer end surface of the drying tower (111), the exhaust hole (108) is in communication with the inner wall of the drying chamber (122), and an on-off valve (109) is provided in the exhaust hole (108).

7. A novel zero-gas consumption adsorption dryer according to claim 1, characterized in that: An air flow detector (112) is provided at the top of the drying tower (111), and the air flow detector (112) is capable of detecting the flow rate of gas flowing through the product gas pipe (113).

8. A novel zero-gas consumption adsorption dryer according to claim 1, characterized in that: The front end of the air pump group (118) is connected to a flow divider (119), and two side end surfaces of the flow divider (119) are connected to two flow divider pipes (120).

9. A novel zero-gas consumption adsorption dryer according to claim 1, characterized in that: Stable supports (105) are fixedly provided at both ends of the support base (101), and the stable supports (105) on both sides are symmetrically arranged. An input pipe opening (104) is provided at the bottom of the drying tower (111), and the input pipe opening (104) passes through the stable supports (105). The stable supports (105) play a role of stable support.

10. A novel zero-gas consumption adsorption dryer according to claim 9, characterized in that: The input pipe opening (104) is connected to the flow diversion pipe (120) via a connecting pipe.

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