CN204746040U - Horizontal compression heat drying equipment of single tower - Google Patents
Horizontal compression heat drying equipment of single tower Download PDFInfo
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- CN204746040U CN204746040U CN201520476633.XU CN201520476633U CN204746040U CN 204746040 U CN204746040 U CN 204746040U CN 201520476633 U CN201520476633 U CN 201520476633U CN 204746040 U CN204746040 U CN 204746040U
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Abstract
The utility model relates to a compressed air purifies technical field, discloses a horizontal compression heat drying equipment of single tower, including adsorption tower (1) and cooler (2), adsorption tower (1) upside is equipped with first pipeline (3), adsorption tower (1) downside is equipped with second pipeline (4), adsorption tower (1) is including first absorption tower cavity (11) and second absorption tower cavity (12), be equipped with between first absorption tower cavity (11) and second absorption tower cavity (12) two -layer baffle (13), cooler (2) is all connected through second pipeline (4) in first absorption tower cavity (11) and second absorption tower cavity (12), be equipped with filter (5) between second absorption tower cavity and the cooler. The utility model discloses whole integrated level is high, compact structure, occupy small, convenient operation, simultaneously more succinct. First absorption tower cavity and second absorption tower cavity all have the reposition of redundant personnel cap from top to bottom, and the reposition of redundant personnel cap makes the compressed air evenly distributed's that gets into the whole cavity that pass through, and the central velocity of flow of the cavity that slows down reaches better adsorption effect.
Description
Technical field
The utility model relates to compressed air purifying technical field, has particularly related to the horizontal compression hot drying equipment of a kind of single tower.
Background technology
The reduction of energy consumption is now eternal in the world topic, namely improves high-energy equipment.Due to the restriction of installing space, cannot the lower heat of compression absorption drier of Energy in use when existing air compression station carries out transforming or increase equipment.
Summary of the invention
The utility model, for the shortcoming of prior art, provides the horizontal compression hot drying equipment of a kind of single tower.
In order to solve the problems of the technologies described above, the utility model is solved by following technical proposals:
The horizontal compression hot drying equipment of single tower, comprise adsorption tower and cooler, the first pipeline is provided with on the upside of adsorption tower, the second pipeline is provided with on the downside of adsorption tower, adsorption tower comprises the first absorption tower chamber and second absorption tower chamber, be provided with two-layer dividing plate between first absorption tower chamber and second absorption tower chamber, the first absorption tower chamber is all connected cooler by the second pipeline with second absorption tower chamber, is provided with filter between second absorption tower chamber and cooler.
In the utility model, adsorption tower inside uses dividing plate to be divided into two desiccant cavitys (i.e. the first absorption tower chamber and second absorption tower chamber), forms the areola that needs to fill temperature insulating material between two-layer dividing plate.The utility model only needs use adsorption tower.Adsorption tower inside adopts two-layer dividing plate to separate.The sleeping placement of lying of adsorption tower list tower of the present utility model.
As preferably, the first absorption tower chamber and second absorption tower chamber madial wall are equipped with shunting cap.First absorption tower chamber and second absorption tower chamber all have shunting cap up and down, and shunting cap makes the compressed air that enters equally distributed by whole cavity, and slow down chamber central flow velocity, reaches better adsorption effect.
As preferably, between two-layer dividing plate, be provided with heat-barrier material.The utility model only needs use adsorption tower.Adsorption tower inside adopts two-layer dividing plate to separate, filling with insulation material between dividing plate.
As preferably, the second pipeline is connected with muffler.
As preferably, cooler comprises the first branch road, the second branch road and the 3rd branch road, and the first branch road is connected with the first pneumatic operated valve, and the second branch road is connected with the first absorption tower chamber, and the 3rd branch road is connected with second absorption tower chamber.
As preferably, also include an inlet and an outlet, entrance connects the first pneumatic operated valve and the first absorption tower chamber respectively, is provided with the first pipeline between entrance and the first absorption tower chamber; Outlet connects the first absorption tower chamber and second absorption tower chamber respectively by the first pipeline.
First pipeline comprises control Compressed Gas and passes into the pneumatic operated valve of the first absorption tower chamber and control the pneumatic operated valve that gas passes into second absorption tower chamber.Second pipeline comprises control Compressed Gas and passes into the pneumatic operated valve of the first absorption tower chamber and control the pneumatic operated valve that gas passes into second absorption tower chamber.The utility model adopts PLC to control whole pneumatic operated valve, can distinguish pressurising, pressure release, and complete the operations such as double tower (i.e. the first absorption tower chamber and second absorption tower chamber) absorption simultaneously to the first absorption tower chamber and second absorption tower chamber.
The utility model, owing to have employed above technical scheme, has significant technique effect: the utility model over all Integration degree is high, and compact conformation takies volume little, easy to operate, simultaneously more succinct.The utility model only needs use adsorption tower, adsorption tower inside uses dividing plate to be divided into two desiccant cavitys (i.e. the first absorption tower chamber and second absorption tower chamber), forms the areola that needs to fill temperature insulating material between two-layer dividing plate; Reduce overall volume, reduce energy consumption, ensure dew point performance, the horizontal compression heat dryer of single tower of the present utility model can support the use with oil free screw air compressor machine and little centrifugal air compressor.First absorption tower chamber and second absorption tower chamber all have shunting cap up and down, and shunting cap makes the compressed air that enters equally distributed by whole cavity, and slow down chamber central flow velocity, reaches better adsorption effect.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
Below in conjunction with accompanying drawing and embodiment, the utility model is described in further detail.
Embodiment 1
The horizontal compression hot drying equipment of single tower, as shown in Figure 1, comprises adsorption tower 1 and cooler 2, is provided with the first pipeline 3 on the upside of adsorption tower 1, be provided with the second pipeline 4, second pipeline 4 and be connected with muffler 6 on the downside of adsorption tower 1.Adsorption tower 1 comprises the first absorption tower chamber 11 and second absorption tower chamber 12, first absorption tower chamber 11 and second absorption tower chamber 12 madial wall and is equipped with shunting cap 14.Be provided with two-layer dividing plate 13 between first absorption tower chamber 11 and second absorption tower chamber 12, between two-layer dividing plate 13, be provided with heat-barrier material 15.First absorption tower chamber 11 and second absorption tower chamber 12 are all connected cooler 2 by the second pipeline 4, are provided with filter 5 between second absorption tower chamber and cooler.
Cooler 2 comprises the first branch road 21, second branch road 22 and the 3rd branch road 23, first branch road 21 and is connected with the first pneumatic operated valve 7, second branch road 22 and is connected with the first absorption tower chamber 11, and the 3rd branch road 23 is connected with second absorption tower chamber 12.Also comprise entrance 8 and outlet 9, entrance 8 connects the first pneumatic operated valve 7 and the first absorption tower chamber 11 respectively, is provided with the first pipeline 3 between entrance 8 and the first absorption tower chamber 11; Outlet 9 connects the first absorption tower chamber 11 and second absorption tower chamber 12 respectively by the first pipeline 3.
Embodiment 2
Embodiment 2 is with the difference of embodiment 1: the first pipeline 3 comprises and controls pneumatic operated valve that Compressed Gas passes into the first absorption tower chamber 11 and control the pneumatic operated valve that gas passes into second absorption tower chamber 12.Second pipeline 4 comprises control Compressed Gas and passes into the pneumatic operated valve of the first absorption tower chamber 11 and control the pneumatic operated valve that gas passes into second absorption tower chamber 12.Adopt PLC to control whole pneumatic operated valve, pressurising, pressure release can be distinguished to the first absorption tower chamber 11 and second absorption tower chamber 12, and complete the operations such as double tower (i.e. the first absorption tower chamber and second absorption tower chamber) absorption simultaneously.
Embodiment 3
Embodiment 3 is with the difference of embodiment 1: the first pipeline 3 comprises the second pneumatic operated valve 31, the 3rd Pneumatic valve 32, the 4th Pneumatic valve 33, the 8th Pneumatic valve 34, equalizer valve 35.Second pipeline 4 comprises the 5th pneumatic operated valve 41, the 6th Pneumatic valve 42, the 7th Pneumatic valve 43, the 9th Pneumatic valve 44.
This equipment working state has several:
1. the first absorption tower chamber 11 regenerates, and second absorption tower chamber 12 adsorbs.
Hot and humid compressed air enters the first absorption tower chamber 11 pairs of adsorbents through the second pneumatic operated valve 31 and carries out hot recycling, then enter cooler 2 by the 5th pneumatic operated valve 41 to lower the temperature, be removed by the aqueous water comprised in the mixing wastewater with air fluid of a large amount of water droplet after cooler 2, then enter second absorption tower chamber 12 through the 6th Pneumatic valve 42, then be supplied to client's gas through the 3rd Pneumatic valve 32 from outlet 9.
2. the first absorption tower chamber 11 pressure release, second absorption tower chamber 12 adsorbs.
Hot and humid compressed air enters cooler 2 through the first pneumatic operated valve 7 and lowers the temperature, be removed by the aqueous water comprised in the mixing wastewater with air fluid of a large amount of water droplet after cooler 2, then the 6th Pneumatic valve 42 enters second absorption tower chamber 12, then is supplied to client's gas through the 3rd Pneumatic valve 32 from outlet 9.Compressed air simultaneously in the first absorption tower chamber 11 through the 7th Pneumatic valve 43, then carries out pressure release through muffler 6.
3. the first absorption tower chamber 11 cold blowing, second absorption tower chamber 12 adsorbs.
Hot and humid compressed air enters cooler 2 through the first pneumatic operated valve 7 and lowers the temperature, be removed by the aqueous water comprised in the mixing wastewater with air fluid of a large amount of water droplet after cooler 2, then enter second absorption tower chamber 12 through the 6th Pneumatic valve 42, then be supplied to client's gas through the 3rd Pneumatic valve 32 from outlet 9.4th Pneumatic valve the 33, eight Pneumatic valve 34 is opened simultaneously, enters the first absorption tower chamber 11 after small part finished product compressed air is extracted through the 4th Pneumatic valve 33 and the 8th Pneumatic valve 34, then discharges with muffler 6 through the 7th Pneumatic valve 43.
4. the first absorption tower chamber 11 is waited for, second absorption tower chamber 12 adsorbs.
Hot and humid compressed air enters cooler 2 through the first pneumatic operated valve 7 and lowers the temperature, be removed by the aqueous water comprised in the mixing wastewater with air fluid of a large amount of water droplet after cooler 2, then enter second absorption tower chamber 12 through the 6th Pneumatic valve 42, then be supplied to client's gas through the 3rd Pneumatic valve 32.Equalizer valve 35 is opened simultaneously, and the first absorption tower chamber 11 carries out pressurising, enters wait state simultaneously.
5. the first absorption tower chamber 11 adsorbs, and second absorption tower chamber 12 adsorbs.
Hot and humid compressed air enters cooler 2 through the first pneumatic operated valve 7 and lowers the temperature, be removed by the aqueous water comprised in the mixing wastewater with air fluid of a large amount of water droplet after cooler 2, then enter the first absorption tower chamber 11 and second absorption tower chamber 12 through the 6th Pneumatic valve 42 and the 9th Pneumatic valve 44 simultaneously, then be supplied to client's gas through the 3rd Pneumatic valve 32 and the tenth Pneumatic valve 35.
6. the first absorption tower chamber 11 adsorbs, and second absorption tower chamber 12 regenerates.
Now replying state has arrived the first state, but the first absorption tower chamber 11 and second absorption tower chamber 12 have switched, switch successively, ensures the safety of whole adsorption process and the stable of end product gas dew point.
In a word, the foregoing is only preferred embodiment of the present utility model, all equalizations done according to the utility model claim change and modify, and all should belong to the covering scope of the utility model patent.
Claims (6)
1. the horizontal compression hot drying equipment of single tower, it is characterized in that: comprise adsorption tower (1) and cooler (2), adsorption tower (1) upside is provided with the first pipeline (3), adsorption tower (1) downside is provided with the second pipeline (4), adsorption tower (1) comprises the first absorption tower chamber (11) and second absorption tower chamber (12), two-layer dividing plate (13) is provided with between first absorption tower chamber (11) and second absorption tower chamber (12), first absorption tower chamber (11) is all connected cooler (2) by the second pipeline (4) with second absorption tower chamber (12), filter (5) is provided with between second absorption tower chamber and cooler.
2. the horizontal compression hot drying equipment of the single tower of one according to claim 1, is characterized in that: the first absorption tower chamber (11) and second absorption tower chamber (12) madial wall are equipped with shunting cap (14).
3. the horizontal compression hot drying equipment of the single tower of one according to claim 1, is characterized in that: be provided with heat-barrier material (15) between two-layer dividing plate (13).
4. the horizontal compression hot drying equipment of the single tower of one according to claim 1, is characterized in that: the second pipeline (4) is connected with muffler (6).
5. the horizontal compression hot drying equipment of the single tower of one according to claim 1, it is characterized in that: cooler (2) comprises the first branch road (21), the second branch road (22) and the 3rd branch road (23), first branch road (21) is connected with the first pneumatic operated valve (7), second branch road (22) is connected with the first absorption tower chamber (11), and the 3rd branch road (23) is connected with second absorption tower chamber (12).
6. the horizontal compression hot drying equipment of the single tower of one according to claim 5, it is characterized in that: also comprise entrance (8) and outlet (9), entrance (8) connects the first pneumatic operated valve (7) and the first absorption tower chamber (11) respectively, is provided with the first pipeline (3) between entrance (8) and the first absorption tower chamber (11); Outlet (9) connects the first absorption tower chamber (11) and second absorption tower chamber (12) respectively by the first pipeline (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520476633.XU CN204746040U (en) | 2015-06-30 | 2015-06-30 | Horizontal compression heat drying equipment of single tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520476633.XU CN204746040U (en) | 2015-06-30 | 2015-06-30 | Horizontal compression heat drying equipment of single tower |
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|---|---|
| CN204746040U true CN204746040U (en) | 2015-11-11 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520476633.XU Active CN204746040U (en) | 2015-06-30 | 2015-06-30 | Horizontal compression heat drying equipment of single tower |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111135708A (en) * | 2020-01-13 | 2020-05-12 | 山东中创新材料科技有限公司 | Organic waste gas treatment system and method |
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2015
- 2015-06-30 CN CN201520476633.XU patent/CN204746040U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111135708A (en) * | 2020-01-13 | 2020-05-12 | 山东中创新材料科技有限公司 | Organic waste gas treatment system and method |
| CN111135708B (en) * | 2020-01-13 | 2022-02-08 | 山东中创新材料科技有限公司 | Organic waste gas treatment system and method |
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