CN209348383U - A kind of efficiently renewable absorption type dryer - Google Patents
A kind of efficiently renewable absorption type dryer Download PDFInfo
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- CN209348383U CN209348383U CN201821596331.6U CN201821596331U CN209348383U CN 209348383 U CN209348383 U CN 209348383U CN 201821596331 U CN201821596331 U CN 201821596331U CN 209348383 U CN209348383 U CN 209348383U
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- adsorption tower
- regeneration
- pipeline
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Abstract
The utility model provides a kind of efficiently renewable absorption type dryer, comprising: left adsorption tower and right adsorption tower；The both ends of lower pipeline, lower pipeline are connected to left adsorption tower with the lower end of right adsorption tower respectively；Two intake valves being located on lower pipeline；Air inlet pipe；Lower regenerating tube, the both ends of lower regenerating tube are connected to lower pipeline respectively, and two intake valves are located between the both ends of lower regenerating tube；Two lower regeneration valves being located on lower regenerating tube；Regenerate escape pipe；The upper pipeline that both ends are connected to left adsorption tower with the upper end of right adsorption tower respectively；Two air outlet valves being located on pipeline；Escape pipe；The upper regenerating tube that both ends are connected to upper pipeline respectively, two air outlet valves are located between the both ends of upper regenerating tube；It is located at regeneration valve on two on regenerating tube；Air inlet pipe is regenerated, the one end for regenerating air inlet pipe is connected to upper regenerating tube；Air blower and heater, heater are used for the air of heater blower sucking.The desiccant dryness air and favorable regeneration effect, speed are fast.
Description
Technical field
The utility model relates to the renewable absorption type dryer technical fields of Efficient air, in particular to one kind efficiently can be again
Raw absorption type dryer.
Background technique
The air or gas of clean dried is gas source important in industrial production, the clean level or drying of air or gas
Degree has great influence to industrial production, for example, production technology or product quality may be influenced.Existing air or gas is dry
Although dry machine can satisfy the dry of common air or gas and require, but existing drying machine drying efficiency is low, adsorbent
Regeneration effect is bad, and reproduction speed is slow, and energy consumption is high, cannot be dried simultaneously and the regeneration of desiccant, brings not to production
Just.
Utility model content
In view of this, the present invention provides a kind of efficiently renewable absorption type dryers.
In order to solve the above technical problems, the utility model uses following technical scheme:
According to the efficient renewable absorption type dryer of the utility model embodiment, comprising:
Left adsorption tower and right adsorption tower；
Lower pipeline, the both ends of the lower pipeline are connected to the left adsorption tower with the lower end of the right adsorption tower respectively；
Two intake valves, two intake valves are respectively provided on the lower pipeline；
Air inlet pipe, one end of the air inlet pipe is connected to the lower pipeline and is located between two intake valves, described
The other end of air inlet pipe with compressor for being connected；
Lower regenerating tube, the both ends of the lower regenerating tube are connected to the lower pipeline respectively, and two intake valves are located at institute
State the position between the both ends of lower regenerating tube；
Two lower regeneration valves, two lower regeneration valves are respectively provided on the lower regenerating tube；
Escape pipe is regenerated, one end of the regeneration escape pipe is connected to the lower regenerating tube and is located at two lower regeneration
Position between valve；
Upper pipeline, the both ends of the upper pipeline are connected to the left adsorption tower with the upper end of the right adsorption tower respectively；
Two air outlet valves, two air outlet valves are respectively provided on the upper pipeline；
Escape pipe, one end of the escape pipe are connected to the upper pipeline and are located between two air outlet valves；
Upper regenerating tube, the both ends of the upper regenerating tube are connected to the upper pipeline respectively, and two air outlet valves are located at institute
State the position between the both ends of regenerating tube；
Two upper regeneration valves, two upper regeneration valves are respectively provided on the upper regenerating tube；
Air inlet pipe is regenerated, one end of the regeneration air inlet pipe is connected to the upper regenerating tube and is located at two upper regeneration
Position between valve；
Air blower and heater, the air blower are located at the other end of the regeneration air inlet pipe, and the heater is located at institute
The middle part of regeneration air inlet pipe is stated, the heater is used to heat the air of the air blower sucking.
Further, the efficiently renewable absorption type dryer further include:
The other end of connecting tube, the regeneration air inlet pipe is connected to the connecting tube；
Two connection valves, two connection valves are located in the connecting tube and the other end of the regeneration air inlet pipe is located at
Position between two connection valves；
One end of the connecting tube is connected to the other end of the regeneration escape pipe, one of them described connection valve is located at institute
State the position between the other end of regeneration air inlet pipe and the other end of the regeneration escape pipe.
Further, the efficiently renewable absorption type dryer further include:
Compressor, the air outlet of the compressor are connected to the other end of the air inlet pipe.
Further, the efficiently renewable absorption type dryer further include:
Pedestal, the left adsorption tower and the right adsorption tower are respectively provided on the pedestal.
Further, the efficiently renewable absorption type dryer further include:
Traveling wheel, the traveling wheel are located at the bottom of the pedestal.
Further, the efficiently renewable absorption type dryer further include:
Insulating layer, the insulating layer are laid in respectively on the outside of the left adsorption tower and the right adsorption tower.
Further, the left adsorption tower includes left tank body and left adsorbent, and the left adsorbent is mounted in the left tank body
In；
The right adsorption tower includes right tank body and right adsorbent, and the right adsorbent is in the right tank body；
The both ends of the lower pipeline are connected to the left tank body with the lower end of the right tank body respectively；
The both ends of the upper pipeline are connected to the left tank body with the upper end of the right tank body respectively.
Further, the efficiently renewable absorption type dryer further include:
Two lower pressure gauges, the both ends of the lower pipeline are respectively equipped with the lower pressure gauge, be respectively used to measurement from
The air pressure that the lower end of the left adsorption tower and the right adsorption tower passes in and out；
Two upper pressure gauges, the both ends of the upper pipeline are respectively equipped with the upper pressure gauge, be respectively used to measurement from
The air pressure that the upper end of the left adsorption tower and the right adsorption tower passes in and out.
The above-mentioned technical proposal of the utility model has the beneficial effect that:
According to the efficient renewable absorption type dryer of the utility model embodiment, pass through the connection of pipeline and valve
Switching, left adsorption tower and right adsorption tower independently can be adsorbed by drying or be regenerated, can also be dried or regenerate simultaneously, mention
The drying efficiency of high air, desiccant regeneration effect is good, and reproduction speed is fast, and low energy consumption, can be improved dry empty in industrial production
The supply of gas, the desiccant structure is simple, easy to manufacture.
Detailed description of the invention
Fig. 1 is the connection schematic diagram of the efficient renewable absorption type dryer of the utility model embodiment.
Appended drawing reference:
Efficient renewable absorption type dryer 100；
Left adsorption tower 10；
Right adsorption tower 20；
Lower pipeline 30；Intake valve 31；Air inlet pipe 32；Lower regenerating tube 33；
Lower regeneration valve 34；Regenerate escape pipe 35；Lower pressure gauge 36；
Upper pipeline 40；Air outlet valve 41；Escape pipe 42；Upper regenerating tube 43；
Upper regeneration valve 44；Regenerate air inlet pipe 45；Upper pressure gauge 46；
Air blower 50；Heater 51；
Connecting tube 60；Connection valve 61；
Compressor 70.
Specific embodiment
It is practical new below in conjunction with this to keep the objectives, technical solutions, and advantages of the embodiments of the present invention clearer
The technical solution of the utility model embodiment is clearly and completely described in the attached drawing of type embodiment.Obviously, described
Embodiment is a part of the embodiment of the utility model, instead of all the embodiments.Based on described the utility model
Embodiment, those of ordinary skill in the art's every other embodiment obtained, fall within the protection scope of the utility model.
The efficient renewable absorption type dryer 100 according to the utility model embodiment is specifically described with reference to the accompanying drawing.
As shown in Figure 1, the efficient renewable absorption type dryer 100 according to the utility model embodiment includes:
Left adsorption tower 10 and right adsorption tower 20；
Lower pipeline 30, the both ends of lower pipeline 30 are connected to left adsorption tower 10 with the lower end of right adsorption tower 20 respectively；
Two intake valves 31, two intake valves 31 are respectively provided on lower pipeline 30；
Air inlet pipe 32, one end of air inlet pipe 32 are connected to and are located between two intake valves 31, air inlet pipe 32 with lower pipeline 30
The other end for being connected with compressor；
Lower regenerating tube 33, the both ends of lower regenerating tube 33 are connected to lower pipeline 30 respectively, and two intake valves 31 are located at lower regeneration
Position between the both ends of pipe 33；
Two lower regeneration valves 34, two lower regeneration valves 34 are respectively provided on lower regenerating tube 33；
Regenerate escape pipe 35, the one end for regenerating escape pipe 35 be connected to lower regenerating tube 33 and positioned at two lower regeneration valves 34 it
Between position；
Upper pipeline 40, the both ends of upper pipeline 40 are connected to left adsorption tower 10 with the upper end of right adsorption tower 20 respectively；
Two air outlet valves 41, two air outlet valves 41 are respectively provided on pipeline 40；
Escape pipe 42, one end of escape pipe 42 are connected to upper pipeline 40 and are located between two air outlet valves 41；
Upper regenerating tube 43, the both ends of upper regenerating tube 43 are connected to upper pipeline 40 respectively, and two air outlet valves 41 are located at upper regeneration
Position between the both ends of pipe 43；
Two upper regeneration valves 44, two upper regeneration valves 44 are respectively provided on regenerating tube 43；
Regenerate air inlet pipe 45, the one end for regenerating air inlet pipe 45 be connected to upper regenerating tube 43 and gone up positioned at two regeneration valves 44 it
Between position；
Air blower 50 and heater 51, air blower 50 are located at the other end of regeneration air inlet pipe 45, and heater 51 is located at regeneration
The middle part of air inlet pipe 45, heater 51 are used for the air that heater blower 50 sucks.The sucking of 51 heater blower 50 of heater
After air, high temperature air enters in adsorption tower the vaporization that can accelerate water on adsorbent, accelerates regeneration.
In some embodiments, efficient renewable absorption type dryer 100 further include:
The other end of connecting tube 60, regeneration air inlet pipe 45 is connected to connecting tube 60；
Two connection valves 61, two connection valves 61 are located at the other end in connecting tube 60 and regenerating air inlet pipe 45 positioned at two
Position between connection valve 61；
One end of connecting tube 60 is connected to the other end of regeneration escape pipe 35, and one of connection valve 61 is located at regeneration air inlet
Position between the other end of pipe 45 and the other end for regenerating escape pipe 35.
In further embodiments, efficient renewable absorption type dryer 100 further include:
The air outlet of compressor 70, compressor 70 is connected to the other end of air inlet pipe 32.
Some embodiments according to the present utility model, efficient renewable absorption type dryer 100 further include:
Pedestal, left adsorption tower 10 and right adsorption tower 20 are respectively provided on pedestal.
Other embodiments according to the present utility model, efficient renewable absorption type dryer 100 further include:
Traveling wheel, traveling wheel are located at the bottom of pedestal.
Preferably, efficient renewable absorption type dryer 100 further include:
Insulating layer, insulating layer are laid in respectively on the outside of left adsorption tower 10 and right adsorption tower 20, are reduced inside adsorption tower with outside
The heat of boundary's environment exchanges, and reduces influence of the external environment to adsorption tower internal temperature.
In certain embodiments, left adsorption tower 10 includes left tank body and left adsorbent, and left adsorbent is mounted in left tank body
In；
Right adsorption tower 20 includes right tank body and right adsorbent, and right adsorbent is in right tank body；
The both ends of lower pipeline 30 are connected to left tank body with the lower end of right tank body respectively；
The both ends of upper pipeline 40 are connected to left tank body with the upper end of right tank body respectively.
In other specific embodiments, efficient renewable absorption type dryer 100 further include:
Two lower pressure gauges 36, the both ends of lower pipeline 30 are respectively equipped with a lower pressure gauge 36, are respectively used to measurement from a left side
The air pressure that the lower end of adsorption tower 10 and right adsorption tower 20 passes in and out；
Two upper pressure gauges 46, the both ends of upper pipeline 40 are respectively equipped with a upper pressure gauge 46, are respectively used to measurement from a left side
The air pressure that the upper end of adsorption tower 10 and right adsorption tower 20 passes in and out.
In use, it as shown in Figure 1, when dry air is dried in left adsorption tower 10, opens on lower pipeline 30
The left side intake valve 31, close the intake valve 31 on the right, close the lower regeneration valve 34 on the left side on lower regenerating tube 33, in opening
The air outlet valve 41 on the left side on pipeline 40 can close the air outlet valve 41 on the right, the left side in closing on regenerating tube 43 it is upper again
Raw valve 44, the air that compressor 70 sucks can enter in left adsorption tower 10 from the lower end of left adsorption tower 10, and left adsorption tower 10 is right
After air is adsorbed by drying, the air after drying is flowed out from the upper end of left adsorption tower 10, is then flowed out from escape pipe 42, with
Dry air is provided for subsequent handling.
When left adsorption tower 10 regenerates, the connection valve 61 on the left side in connecting tube 60 is opened, closes the connection valve 61 on the right, is opened
The upper regeneration valve 44 on the left side closes the upper regeneration valve 44 on the right, closes the air outlet valve 41 on the left side, close the intake valve 31 on the left side,
The lower regeneration valve 34 for opening the left side closes the lower regeneration valve 34 on the right.The air that air blower 50 sucks is heated by heater 51
Enter in left adsorption tower 10 from the upper end of left adsorption tower 10 afterwards, the water in left adsorption tower 10 on adsorbent carries out under high temperature air
Vaporization is flowed out under the drive of air from the lower end of left adsorption tower 10, then after lower regenerating tube 33 and regeneration escape pipe 35
It flows out from the right end of connecting tube 60, so that the steam in left adsorption tower 10 be taken out of, realizes to adsorbent in left adsorption tower 10
Regeneration, after the completion of regeneration, left adsorption tower 10 can continue the drying of air.
The drying of right adsorption tower 20 and regenerative process are identical as the Principle of Process of left adsorption tower 10, and details are not described herein, can
While to realize that left adsorption tower 10 is dry by the valve transfer on pipeline, right adsorption tower 20 regenerates, can also two absorption
Tower is dry simultaneously or regenerates.Particular condition in use can switch over adjusting according to needs of production.
According to the efficient renewable absorption type dryer 100 of the utility model embodiment, connection and valve by pipeline
The switching of door, left adsorption tower 10 and right adsorption tower 20 independently can be adsorbed by drying or be regenerated, can also be dried simultaneously
Or regeneration, the drying efficiency of air is improved, desiccant regeneration effect is good, and reproduction speed is fast, and low energy consumption, can be improved industrial production
The supply of middle dry air, the desiccant structure is simple, easy to manufacture.
The above is preferred embodiments of the present invention, it is noted that for the ordinary skill of the art
For personnel, under the premise of not departing from principle described in the utility model, it can also make several improvements and retouch, these improvement
It also should be regarded as the protection scope of the utility model with retouching.
Claims (7)
1. a kind of efficiently renewable absorption type dryer characterized by comprising
Left adsorption tower and right adsorption tower；
Lower pipeline, the both ends of the lower pipeline are connected to the left adsorption tower with the lower end of the right adsorption tower respectively；
Two intake valves, two intake valves are respectively provided on the lower pipeline；
Air inlet pipe, one end of the air inlet pipe are connected to and are located between two intake valves, the air inlet with the lower pipeline
The other end of pipe with compressor for being connected；
Lower regenerating tube, the both ends of the lower regenerating tube are connected to the lower pipeline respectively, two intake valves be located at it is described under
Position between the both ends of regenerating tube；
Two lower regeneration valves, two lower regeneration valves are respectively provided on the lower regenerating tube；
Regenerate escape pipe, one end of the regeneration escape pipe be connected to the lower regenerating tube and positioned at two lower regeneration valves it
Between position；
Upper pipeline, the both ends of the upper pipeline are connected to the left adsorption tower with the upper end of the right adsorption tower respectively；
Two air outlet valves, two air outlet valves are respectively provided on the upper pipeline；
Escape pipe, one end of the escape pipe are connected to the upper pipeline and are located between two air outlet valves；
Upper regenerating tube, the both ends of the upper regenerating tube are connected to the upper pipeline respectively, and two air outlet valves are located on described
Position between the both ends of regenerating tube；
Two upper regeneration valves, two upper regeneration valves are respectively provided on the upper regenerating tube；
Regenerate air inlet pipe, one end of the regeneration air inlet pipe be connected to the upper regenerating tube and positioned at two upper regeneration valves it
Between position；
Air blower and heater, the air blower are located at the other end of the regeneration air inlet pipe, the heater be located at it is described again
The middle part of raw air inlet pipe, the heater are used to heat the air of the air blower sucking；
Further include:
Insulating layer, the insulating layer are laid in respectively on the outside of the left adsorption tower and the right adsorption tower.
2. efficiently renewable absorption type dryer according to claim 1, which is characterized in that further include:
The other end of connecting tube, the regeneration air inlet pipe is connected to the connecting tube；
Two connection valves, two connection valves are located in the connecting tube and the other end of the regeneration air inlet pipe is located at two
Position between the connection valve；
One end of the connecting tube with it is described regeneration escape pipe the other end be connected to, one of them described connection valve be located at described in again
Position between the other end of raw air inlet pipe and the other end of the regeneration escape pipe.
3. efficiently renewable absorption type dryer according to claim 1, which is characterized in that further include:
Compressor, the air outlet of the compressor are connected to the other end of the air inlet pipe.
4. efficiently renewable absorption type dryer according to claim 1, which is characterized in that further include:
Pedestal, the left adsorption tower and the right adsorption tower are respectively provided on the pedestal.
5. efficiently renewable absorption type dryer according to claim 4, which is characterized in that further include:
Traveling wheel, the traveling wheel are located at the bottom of the pedestal.
6. efficiently renewable absorption type dryer according to claim 1, which is characterized in that the left adsorption tower includes a left side
Tank body and left adsorbent, the left adsorbent is in the left tank body；
The right adsorption tower includes right tank body and right adsorbent, and the right adsorbent is in the right tank body；
The both ends of the lower pipeline are connected to the left tank body with the lower end of the right tank body respectively；
The both ends of the upper pipeline are connected to the left tank body with the upper end of the right tank body respectively.
7. efficiently renewable absorption type dryer according to claim 1, which is characterized in that further include:
Two lower pressure gauges, the both ends of the lower pipeline are respectively equipped with the lower pressure gauge, are respectively used to measure from described
The air pressure that the lower end of left adsorption tower and the right adsorption tower passes in and out；
Two upper pressure gauges, the both ends of the upper pipeline are respectively equipped with the upper pressure gauge, are respectively used to measure from described
The air pressure that the upper end of left adsorption tower and the right adsorption tower passes in and out.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821596331.6U CN209348383U (en) | 2018-09-29 | 2018-09-29 | A kind of efficiently renewable absorption type dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821596331.6U CN209348383U (en) | 2018-09-29 | 2018-09-29 | A kind of efficiently renewable absorption type dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209348383U true CN209348383U (en) | 2019-09-06 |
Family
ID=67781777
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821596331.6U Expired - Fee Related CN209348383U (en) | 2018-09-29 | 2018-09-29 | A kind of efficiently renewable absorption type dryer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209348383U (en) |
-
2018
- 2018-09-29 CN CN201821596331.6U patent/CN209348383U/en not_active Expired - Fee Related
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| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190906 Termination date: 20210929 |
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| CF01 | Termination of patent right due to non-payment of annual fee |