CN216092993U - Energy-saving zero-gas-consumption micro-thermal regeneration suction dryer - Google Patents
Energy-saving zero-gas-consumption micro-thermal regeneration suction dryer Download PDFInfo
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- CN216092993U CN216092993U CN202122713273.9U CN202122713273U CN216092993U CN 216092993 U CN216092993 U CN 216092993U CN 202122713273 U CN202122713273 U CN 202122713273U CN 216092993 U CN216092993 U CN 216092993U
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Abstract
The utility model discloses an energy-saving zero-gas-consumption micro-thermal regeneration suction dryer which comprises a workbench, an adsorption cylinder and a cooling cylinder, wherein the adsorption cylinder is installed on one side of the upper end of the workbench, the cooling cylinder is installed on the other side of the upper end of the workbench, and the workbench is connected with the adsorption cylinder and the cooling cylinder through bolts. Has the advantages that: according to the utility model, through the design of the air inlet pipe, the fan and the heater, the moisture removing work of the suction dryer can be carried out in a hot air drying mode, so that the influence of the suction dryer on the adsorption capacity of a drying agent in the moisture removing work is avoided, the use effect of the suction dryer is further improved, and through the design of the cooling cylinder, the heat exchanger and the heat exchange pipeline, the suction dryer can have a heat recovery function, so that the suction dryer can recover heat when cooling wet and hot air, and a large amount of thermal resources can be saved.
Description
Technical Field
The utility model relates to the technical field of suction drying machines, in particular to an energy-saving zero-gas-consumption micro-thermal regeneration suction drying machine.
Background
The zero gas consumption micro-heating regeneration suction dryer is an energy-saving compressed air drying device, and adopts the process of blowing and regenerating ambient air, so that a large amount of product gas required by the regeneration of the traditional process can be saved. When heating, the regeneration gas source comes from the ambient air after the pressure of the fan is increased, the ambient air is heated to the regeneration temperature through the heater to be used as the regeneration gas analyzed by the bed layer of the adsorber, and when in regeneration operation, the regeneration heating gas heats and analyzes the adsorption bed layer, carries the water vapor separated out by the regeneration gas and carries the water vapor out of the adsorber to the cooler for dehumidification.
The present dry machine of inhaling mostly adopts the form of pipe wall heating to carry out the dehumidification work, leads to inhaling the dry machine and causing the influence to the adsorption efficiency of drier easily in the dehumidification work to it is relatively poor to cause the result of use of inhaling dry machine, and the dry machine of inhaling that has now simultaneously mostly lacks the heat recovery function, leads to inhaling dry machine can't retrieve the heat when cooling damp and hot air, thereby causes the unnecessary wasting of resources.
SUMMERY OF THE UTILITY MODEL
Technical problem to be solved
In order to overcome prior art not enough, the present energy-saving zero-air-consumption micro-heat regeneration suction dryer is provided, the form that the present suction dryer mostly adopts the pipe wall heating is solved and the dehumidification work is carried out, the adsorption capacity that leads to suction dryer to the drier easily in the dehumidification work causes the influence, thereby the result of use that causes suction dryer is relatively poor, the present suction dryer mostly lacks the heat recovery function simultaneously, lead to suction dryer can't retrieve the heat when cooling wet hot air, thereby cause the problem of unnecessary wasting of resources.
(II) technical scheme
The utility model is realized by the following technical scheme: the utility model provides an energy-saving zero-gas-consumption micro-thermal regeneration suction dryer, which comprises a workbench, an adsorption cylinder and a cooling cylinder, wherein the adsorption cylinder is arranged on one side of the upper end of the workbench, the cooling cylinder is arranged on the other side of the upper end of the workbench, the adsorption cylinder and the cooling cylinder are connected through bolts, communicating pipes are arranged at the upper ends of the adsorption cylinder and the cooling cylinder, the adsorption cylinder and the cooling cylinder are inserted into the communicating pipes, an air inlet pipe is arranged at the lower end of the adsorption cylinder, the adsorption cylinder is inserted into the air inlet pipe, a heater is arranged in the middle of the lower part of the adsorption cylinder, the workbench is connected with the heater through bolts, a fan is arranged at the lower end of the heater, the heater is connected with the fan through screws, a heat exchanger is arranged on the side wall in the cooling cylinder, and the cooling cylinder is connected with the heat exchanger through screws, and a heat exchange pipeline is arranged on one side wall of the heat exchanger.
Furthermore, the pillar is all installed to workstation lower extreme four corners department, the workstation with the pillar passes through bolted connection.
Through adopting above-mentioned technical scheme, can make the suction dryer have more stable operating condition.
Further, a control cabinet is installed in the middle of the upper end of the workbench, and the workbench is connected with the control cabinet through bolts.
Through adopting above-mentioned technical scheme, can make the staff more convenient to control of blotting machine.
Furthermore, a small-particle drying agent is arranged in the middle of the interior of the adsorption cylinder, large-particle drying agents are arranged at the upper end and the lower end of the small-particle drying agent, and the small-particle drying agent and the large-particle drying agents are in lap joint with the adsorption cylinder.
Through adopting above-mentioned technical scheme, can ensure the moisture adsorption effect of blotting machine.
Furthermore, a moisture removal pipe is installed to the cooling cylinder lower extreme, the cooling cylinder with the moisture removal pipe is pegged graft, install the solenoid valve in the moisture removal pipe, the moisture removal pipe with the solenoid valve passes through the screw connection.
Through adopting above-mentioned technical scheme, can make the hydrofuge operation of blotting machine more smooth and easy.
Furthermore, the heat exchange pipeline is inserted into the heat exchanger and penetrates through the cooling cylinder.
Through adopting above-mentioned technical scheme, can make the absorption machine can retrieve the heat when cooling damp and hot air to can practice thrift a large amount of heating power resources.
(III) advantageous effects
Compared with the prior art, the utility model has the following beneficial effects:
1. in order to solve the problem that the existing suction dryer mostly adopts a pipe wall heating mode to carry out dehumidification work, so that the suction dryer is easy to influence the adsorption capacity of a drying agent in the dehumidification work, and the use effect of the suction dryer is poor.
2. In order to solve the problem that most of the existing suction-drying machines lack a heat recovery function, so that the suction-drying machines cannot recover heat when cooling damp and hot air, and unnecessary resources are wasted, the utility model can enable the suction-drying machines to have the heat recovery function through the design of the cooling cylinder, the heat exchanger and the heat exchange pipeline, so that the suction-drying machines can recover heat when cooling the damp and hot air, and a large amount of thermal resources can be saved.
Drawings
FIG. 1 is a schematic structural diagram of an energy-saving zero-gas-consumption micro-thermal regeneration dryer according to the present invention;
FIG. 2 is a cross-sectional view of an energy-saving zero-gas-consumption micro-thermal regeneration dryer according to the present invention;
fig. 3 is a circuit block diagram of the energy-saving zero-gas-consumption micro-thermal regeneration suction dryer of the utility model.
The reference numerals are explained below:
1. a work table; 2. a pillar; 3. an adsorption cylinder; 4. a cooling cylinder; 5. a control cabinet; 6. a communicating pipe; 7. an air inlet pipe; 8. a desiccant screen; 9. a heater; 10. a fan; 11. a small particle desiccant; 12. a large particle desiccant; 13. a moisture removal pipe; 14. an electromagnetic valve; 15. a heat exchanger; 16. a heat exchange conduit; 17. an exhaust pipe; 18. and adjusting the valve.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more apparent, the present invention is described in further detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the utility model and are not intended to limit the utility model.
As shown in fig. 1-3, the energy-saving zero-gas-consumption micro-thermal regeneration dryer in this embodiment includes a workbench 1, an adsorption cylinder 3 and a cooling cylinder 4, the adsorption cylinder 3 is installed on one side of the upper end of the workbench 1, the cooling cylinder 4 is installed on the other side of the upper end of the workbench 1, the adsorption cylinder 3 and the cooling cylinder 4 are all connected by bolts, the communication pipes 6 are installed on the upper ends of the adsorption cylinder 3 and the cooling cylinder 4, the adsorption cylinder 3 and the cooling cylinder 4 are all inserted into the communication pipes 6, the air inlet pipe 7 is installed at the lower end of the adsorption cylinder 3, the adsorption cylinder 3 is inserted into the air inlet pipe 7, the heater 9 is installed at the middle part below the adsorption cylinder 3, the workbench 1 is connected with the heater 9 by bolts, the fan 10 is installed at the lower end of the heater 9, the heater 9 is connected with the fan 10 by screws, the heat exchanger 15 is installed on the side wall inside the cooling cylinder 4, the cooling cylinder 4 is connected with the heat exchanger 15 by screws, a heat exchange pipeline 16 is installed on one side wall of the heat exchanger 15, through the air inlet pipe 7, the fan 10 and the heater 9 are designed, the moisture removal work of the moisture removal machine in a hot air drying mode can be achieved, the influence of the moisture removal machine on the adsorption capacity of a drying agent in the moisture removal work is avoided, the using effect of the moisture removal machine is further improved, the cooling cylinder 4, the heat exchanger 15 and the heat exchange pipeline 16 are designed, the moisture removal machine can be enabled to have a heat recovery function, the moisture removal machine can recover heat when cooling wet and hot air, and a large amount of heat resources can be saved.
As shown in fig. 1-2, in this embodiment, pillars 2 are all installed at four corners of the lower end of the workbench 1, the workbench 1 is connected with the pillars 2 through bolts, the pillars 2 can ensure the stability of the workbench 1, a control cabinet 5 is installed in the middle of the upper end of the workbench 1, the workbench 1 is connected with the control cabinet 5 through bolts, and the control cabinet 5 has an automatic operation function, so that the amount of labor manually controlled by a worker can be reduced.
As shown in fig. 1-2, in the present embodiment, a small-particle desiccant 11 is disposed in the middle of the adsorption cylinder 3, large-particle desiccants 12 are disposed at both upper and lower ends of the small-particle desiccant 11, and both the small-particle desiccant 11 and the large-particle desiccant 12 are overlapped with the adsorption cylinder 3, so that the moisture adsorption effect of the adsorption dryer can be shown.
As shown in fig. 1-2, in this embodiment, a humidity exhaust pipe 13 is installed at the lower end of a cooling cylinder 4, the cooling cylinder 4 is inserted into the humidity exhaust pipe 13, an electromagnetic valve 14 is installed in the humidity exhaust pipe 13, the humidity exhaust pipe 13 is connected with the electromagnetic valve 14 through a screw, a heat exchange pipeline 16 is inserted into a heat exchanger 15, and the heat exchange pipeline 16 penetrates through the cooling cylinder 4, so that the dryer can quickly exhaust moisture after heat recovery.
The specific implementation process of this embodiment is as follows: when the drying device is used, a worker can set the control cabinet 5 firstly, the control cabinet 5 starts the fan 10 to work, the fan 10 can extract outside air into the adsorption cylinder 3 through the air inlet pipe 7, so that the small-particle drying agent 11 and the large-particle drying agent 12 can adsorb water molecules in the air, and the dehumidified air is discharged through the exhaust pipe 17, after the adsorption cylinder 3 works for a long time, when the water contents of the small-particle drying agent 11 and the large-particle drying agent 12 are large, the control cabinet 5 controls the regulating valve 18 to close the exhaust pipe 17 and open the communicating pipe 6, then the fan 10 and the heater 9 are started to work simultaneously, the heater 9 can heat the air extracted by the fan 10, so that hot air enters the adsorption cylinder 3 to perform hot air drying on the small-particle drying agent 11 and the large-particle drying agent 12, and carries precipitated water vapor into the cooling cylinder 4, meanwhile, the heat exchanger 15 continuously absorbs the heat of the damp and hot gas in the cooling cylinder 4, so that the damp and hot gas in the cooling cylinder 4 can be rapidly cooled, then a worker can connect an external pipeline with the humidity discharging pipe 13, and the electromagnetic valve is opened by operating the control cabinet 5, so that the moisture in the cooling cylinder 4 can be rapidly discharged.
The previous description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the generic principles defined herein may be applied to other embodiments without departing from the spirit or scope of the utility model. Thus, the present invention is not intended to be limited to the embodiments shown herein but is to be accorded the widest scope consistent with the principles and novel features disclosed herein. .
Claims (6)
1. An energy-saving zero-gas-consumption micro-thermal regeneration suction dryer is characterized in that: comprises a workbench (1), an adsorption cylinder (3) and a cooling cylinder (4), wherein the adsorption cylinder (3) is installed on one side of the upper end of the workbench (1), the cooling cylinder (4) is installed on the other side of the upper end of the workbench (1), the workbench (1) is connected with the adsorption cylinder (3) and the cooling cylinder (4) through bolts, a communicating pipe (6) is installed on the upper end of the adsorption cylinder (3) and the cooling cylinder (4), the adsorption cylinder (3) and the cooling cylinder (4) are connected with the communicating pipe (6) in an inserting manner, an air inlet pipe (7) is installed at the lower end of the adsorption cylinder (3), the adsorption cylinder (3) is connected with the air inlet pipe (7) in an inserting manner, a heater (9) is installed at the middle part below the adsorption cylinder (3), the workbench (1) is connected with the heater (9) through bolts, a fan (10) is installed at the lower end of the heater (9), the heater (9) with fan (10) pass through the screw connection, all install heat exchanger (15) on the lateral wall in cooling cylinder (4), cooling cylinder (4) with heat exchanger (15) pass through the screw connection, install heat transfer pipeline (16) on a lateral wall of heat exchanger (15).
2. The energy-saving zero-gas-consumption micro-thermal regeneration suction dryer as claimed in claim 1, characterized in that: pillar (2) are all installed to workstation (1) lower extreme four corners department, workstation (1) with pillar (2) pass through bolted connection.
3. The energy-saving zero-gas-consumption micro-thermal regeneration suction dryer as claimed in claim 1, characterized in that: the middle part of the upper end of the workbench (1) is provided with a control cabinet (5), and the workbench (1) is connected with the control cabinet (5) through bolts.
4. The energy-saving zero-gas-consumption micro-thermal regeneration suction dryer as claimed in claim 1, characterized in that: the drying device is characterized in that a small-particle drying agent (11) is arranged in the middle of the interior of the adsorption cylinder (3), large-particle drying agents (12) are arranged at the upper end and the lower end of the small-particle drying agent (11), and the small-particle drying agent (11) and the large-particle drying agent (12) are in lap joint with the adsorption cylinder (3).
5. The energy-saving zero-gas-consumption micro-thermal regeneration suction dryer as claimed in claim 1, characterized in that: the utility model discloses a wet cooling device, including cooling cylinder (4), cooling cylinder (4) lower extreme is installed and is arranged wet pipe (13), cooling cylinder (4) with it pegs graft to arrange wet pipe (13), install solenoid valve (14) in arranging wet pipe (13), arrange wet pipe (13) with solenoid valve (14) pass through the screw connection.
6. The energy-saving zero-gas-consumption micro-thermal regeneration suction dryer as claimed in claim 1, characterized in that: the heat exchange pipeline (16) is inserted into the heat exchanger (15), and the heat exchange pipeline (16) penetrates through the cooling cylinder (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122713273.9U CN216092993U (en) | 2021-11-08 | 2021-11-08 | Energy-saving zero-gas-consumption micro-thermal regeneration suction dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122713273.9U CN216092993U (en) | 2021-11-08 | 2021-11-08 | Energy-saving zero-gas-consumption micro-thermal regeneration suction dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216092993U true CN216092993U (en) | 2022-03-22 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122713273.9U Active CN216092993U (en) | 2021-11-08 | 2021-11-08 | Energy-saving zero-gas-consumption micro-thermal regeneration suction dryer |
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| Country | Link |
|---|---|
| CN (1) | CN216092993U (en) |
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2021
- 2021-11-08 CN CN202122713273.9U patent/CN216092993U/en active Active
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