CN206660907U - Low-grade fever absorption drier - Google Patents
Low-grade fever absorption drier Download PDFInfo
- Publication number
- CN206660907U CN206660907U CN201720338542.9U CN201720338542U CN206660907U CN 206660907 U CN206660907 U CN 206660907U CN 201720338542 U CN201720338542 U CN 201720338542U CN 206660907 U CN206660907 U CN 206660907U
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- CN
- China
- Prior art keywords
- absorption
- heating tube
- cylinder
- low
- grade fever
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
The utility model discloses a kind of low-grade fever absorption drier, including absorption cylinder, external heater, heating tube, temperature inductor, controller, the external heater is connected by high temperature pipe with the absorbing cylinder body phase, the heating tube is in the absorption inner barrel, it is sealedly and fixedly connected with the absorption cylinder, the temperature inductor is fixedly connected, controller electrically connects with the heating tube and temperature inductor with the absorption cylinder in the absorption inner barrel；The utility model adsorbs the gas of inner barrel by constantly heating, and improves the regeneration efficiency of adsorbent, reduces regeneration gas consumption.
Description
Technical field
It the utility model is related to a kind of low-grade fever absorption drier.
Background technology
Its heater of traditional absorption drier is provided in outside, and dry air heats via external heater to be become
Into high-temperature gas, then by pipeline to adsorbing cylinder.Because the scattered temperature of pipeline, and absorption cylinder, adsorbent absorb high temperature
The temperature of gas, therefore high-temperature gas can only be heated to a part for cylinder, heat gas temperatures, tolerance are inadequate, adsorbent
Regeneration efficiency is low, and gas consumption amount is big.
Utility model content
In order to solve the problems, such as that prior art is present, the utility model provides a kind of low-grade fever absorption drier, can not
The interior gas by absorption heat of disconnected heating absorbing cylinder body, improve the regeneration efficiency of adsorbent.
To achieve the above object, the utility model adopts the technical scheme that low-grade fever absorption drier, including：
Adsorb cylinder；
External heater, connected with the absorbing cylinder body phase；
Heating tube, the absorption inner barrel is arranged on, is sealedly and fixedly connected with the absorption cylinder；
Temperature inductor, the absorption inner barrel is arranged on, is fixedly connected with the absorption cylinder；
Controller；Electrically connected with the heating tube and temperature inductor；
Wherein, the heating tube is controlled to heat the absorption inner barrel by the temperature inductor.
In the embodiment of the utility model one, the heating tube includes shell, heater strip, and the heater strip is located at the pipe
In shell, the shell is fixedly connected with the absorption cylinder, and the heater strip electrically connects with the controller.For the ease of changing
Heater strip, heater strip is arranged in shell, when needing to change heater strip, can is easily removed out of absorbing cylinder body
Change, damage is not produced to equipment.
In the embodiment of the utility model one, the heating tube runs through institute along the direction parallel to the absorption tubular axis
State absorption cylinder.The both ends of the shell of heating tube and the barrel sealing welding of absorption cylinder.
In the embodiment of the utility model one, the heating tube is four immerging metal tube heaters, and is symmetrically dispersed in described
In absorbing cylinder body.The gas in sorbent tube body is so caused to be heated evenly.
In the embodiment of the utility model one, the external heater is connected by high temperature pipe with the absorbing cylinder body phase,
The high temperature pipe is connected by the first access port with the absorbing cylinder body phase, and the temperature inductor is located remotely from described first and connect
The absorption inner barrel of entrance.One end that temperature inductor is arranged far from the first access port is advantageous to sense more sensitively
The temperature of gas in absorbing cylinder body so that the gas temperature in absorbing cylinder body is more stable.
The technical program has the advantages that：
By increasing heater strip in absorption inner barrel, make up by equipment, adsorbent to scatter and disappear and the heat that sponges,
The regeneration efficiency of adsorbent is improved, while reduces gas consumption amount, save the energy.When gas temperature drops to and set in absorbing cylinder body
During fixed minimum temperature, the temperature inductor transmits a signal to the controller, and controller is controlled inside the heating tube
Heater strip proceeds by heating；When gas temperature is raised to the maximum temperature of setting in absorbing cylinder body, temperature inductor can pass again
For defeated signal to controller, controller controls the heater strip inside the heating tube to stop heating.
Brief description of the drawings
Fig. 1 is a kind of structural representation of the present utility model；
Fig. 2 is the front view of absorption cylinder of the present utility model；
Fig. 3 is the top view of absorption cylinder of the present utility model；
Fig. 4 is the enlarged drawing of heating tube of the present utility model.
1st, cylinder is adsorbed；2nd, heating tube；3rd, temperature inductor；4th, shell；5th, heater strip；6th, external heater；7th, high temperature
Pipe；8th, the first access port.
Embodiment
It is further described with reference to 1 to 4 pair of the utility model of embodiment and accompanying drawing.
Low-grade fever absorption drier involved by the utility model, including absorption cylinder 1, external heater 6, heating tube 2,
Temperature inductor 3, controller (not shown).The external heater 6 is connected by high temperature pipe 7 with the absorption cylinder 1, institute
State high temperature pipe 7 by the first access port 8 with the absorption cylinder 1 to be connected, the temperature inductor 3 is fixedly mounted on away from institute
State inside the absorption cylinder 1 of the first access port 8.The temperature inductor 3 electrically connects with the controller.The heating tube
2 carry out secondary micro- heating inside the absorption cylinder 1, and the heating tube 2 is along parallel to the direction for adsorbing the axis of cylinder 1
Through the absorption cylinder 1.The heating tube 2 is four immerging metal tube heaters, and is symmetrically dispersed in the absorption cylinder 1.
The heating tube 2 includes shell 4, heater strip 5, and the heater strip 5 is located in the shell 4, the both ends of the shell 4 with it is described
The barrel sealing welding of cylinder 1 is adsorbed, the heater strip 5 electrically connects with the controller., will for the ease of changing heater strip 5
Heater strip 5 is arranged in shell 4, and when needing to change heater strip 5, can easily removes replacing out of absorbing cylinder body, no
Damage is produced to equipment.
The heating tube 2 is controlled to be internally heated the absorption cylinder 1 by the temperature inductor 3.The control
The temperature that device temperature inductor processed detects in the absorption cylinder 1 can send the first signal to institute when reaching the minimum of setting
Controller is stated, the controller controls the heater strip 5 to begin to warm up after receiving first signal；And work as the controller
The temperature that temperature inductor detects in the absorption cylinder 1 can send secondary signal to the control when reaching the peak of setting
Device processed, the controller can control the heater strip 5 to stop heating after receiving the secondary signal.
Because the gas after being heated constantly absorbs heat by cylinder, adsorbent, make the reduction of its temperature, by absorption cylinder
Inside increase heater strip 5, to make up absorbed heat.The utility model is carried by constantly heating by the gas of absorption heat
The high regeneration efficiency of adsorbent, extends the usage time of adsorbent, reduces regeneration gas consumption, saved the energy.
Above-mentioned specific embodiment is used only to illustrate the utility model, rather than is that the utility model is limited,
In objective of the present utility model and scope of the claims, what the utility model was made any does not pay creative labor
Dynamic replacement and change, fall within the protection domain of the utility model patent.
Claims (5)
- A kind of 1. low-grade fever absorption drier, it is characterised in that including：Adsorb cylinder；External heater, connected with the absorbing cylinder body phase；Heating tube, the absorption inner barrel is arranged on, is sealedly and fixedly connected with the absorption cylinder；Temperature inductor, the absorption inner barrel is arranged on, is fixedly connected with the absorption cylinder；Controller；Electrically connected with the heating tube and temperature inductor；Wherein, the heating tube is controlled to heat the absorption inner barrel by the temperature inductor.
- 2. low-grade fever absorption drier according to claim 1, it is characterised in that the heating tube includes shell, heating Silk, the heater strip are located in the shell, and the shell is fixedly connected with the absorption cylinder, the heater strip and the control Device electrical connection processed.
- 3. low-grade fever absorption drier according to claim 2, it is characterised in that the heating tube is along parallel to the suction The absorption cylinder is run through in the direction of attached tubular axis.
- 4. low-grade fever absorption drier according to claim 3, it is characterised in that the heating tube is four METAL HEATING PROCESSs Pipe, and be symmetrically dispersed in the absorbing cylinder body.
- 5. low-grade fever absorption drier according to claim 1, it is characterised in that the external heater passes through high temperature pipe Connected with the absorbing cylinder body phase, the high temperature pipe is connected by the first access port with the absorbing cylinder body phase, the temperature sense Device is answered to be located remotely from the absorption inner barrel of first access port.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720338542.9U CN206660907U (en) | 2017-03-31 | 2017-03-31 | Low-grade fever absorption drier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720338542.9U CN206660907U (en) | 2017-03-31 | 2017-03-31 | Low-grade fever absorption drier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206660907U true CN206660907U (en) | 2017-11-24 |
Family
ID=60367719
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720338542.9U Expired - Fee Related CN206660907U (en) | 2017-03-31 | 2017-03-31 | Low-grade fever absorption drier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206660907U (en) |
-
2017
- 2017-03-31 CN CN201720338542.9U patent/CN206660907U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171124 |