CN207012777U - A kind of energy-efficient drying device of absorption type and system - Google Patents
A kind of energy-efficient drying device of absorption type and system Download PDFInfo
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- CN207012777U CN207012777U CN201720855988.9U CN201720855988U CN207012777U CN 207012777 U CN207012777 U CN 207012777U CN 201720855988 U CN201720855988 U CN 201720855988U CN 207012777 U CN207012777 U CN 207012777U
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- 238000001035 drying Methods 0.000 title claims abstract description 55
- 238000010521 absorption reaction Methods 0.000 title claims abstract description 51
- 230000008929 regeneration Effects 0.000 claims abstract description 22
- 238000011069 regeneration method Methods 0.000 claims abstract description 22
- 239000002245 particle Substances 0.000 claims description 26
- 239000003463 adsorbent Substances 0.000 claims description 17
- 238000001914 filtration Methods 0.000 claims description 16
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 16
- 238000010438 heat treatment Methods 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 239000000428 dust Substances 0.000 claims description 8
- 239000002808 molecular sieve Substances 0.000 claims description 6
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 6
- 229910001220 stainless steel Inorganic materials 0.000 claims description 6
- 239000010935 stainless steel Substances 0.000 claims description 6
- 229910052782 aluminium Inorganic materials 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- 239000004411 aluminium Substances 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 13
- 230000008569 process Effects 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 5
- 239000007789 gas Substances 0.000 description 18
- 238000001816 cooling Methods 0.000 description 13
- 238000001179 sorption measurement Methods 0.000 description 8
- 238000010586 diagram Methods 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 230000008439 repair process Effects 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 229910021389 graphene Inorganic materials 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 239000002594 sorbent Substances 0.000 description 2
- 238000007605 air drying Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000005465 channeling Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000007791 dehumidification Methods 0.000 description 1
- 239000002274 desiccant Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000021715 photosynthesis, light harvesting Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000007420 reactivation Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
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Abstract
The utility model provides a kind of energy-efficient drying device of absorption type, including air inlet and gas outlet, the outlet connection of the air inlet and air compressor machine；The energy-efficient drying device of absorption type also includes the first tub, the second tub and regeneration module；The entrance of first tub is connected by the first intake valve with air inlet pipeline, and the entrance of second tub is connected by the second intake valve with air inlet pipeline；The outlet of first tub is connected by the first air outlet valve with the gas outlet pipeline, and the outlet of second tub is connected by the second air outlet valve with the gas outlet pipeline.The drying device whole flow process not consumption of compressed air, compressed air quality is high, reduces power consumption, energy-saving effect is obvious.
Description
Technical field
The utility model is related to mechanical equipment technical field, more particularly to a kind of energy-efficient drying device of absorption type and
System.
Background technology
Absorption drier is divided into simple type absorption drier（Disposably）With regenerative absorption drier（Automatically follow
It is ring-like）.
Reproduction adsorption type drying machine is made up of two duplex machine barrels, and the drier that can absorb moisture is loaded with machine barrel.Two
Individual machine barrel is switched on or off source of the gas in turn, alternately dries and regenerates operation, so that the drying that air-flow energy continuous contact is dry
Agent come reach dehumidification drying purpose
Air rate is 15% ~ 20% in every profession and trade conventional compression air drying equipment and system work process at present, energy wave
Fei Duo, carbon emission are more.
Utility model content
In order to solve the above technical problems, the utility model provides a kind of energy-efficient drying device of absorption type, it is worked
Compressed air zero is lost in journey, dew point control, extends sorbent life, reduces power consumption, save mass energy.
The utility model provides a kind of energy-efficient drying device of absorption type, including air inlet and gas outlet, it is described enter
The outlet connection of gas port and air compressor machine；
The energy-efficient drying device of absorption type also includes the first tub, the second tub and regeneration module；
The entrance of first tub is connected by the first intake valve with air inlet pipeline, and the entrance of second tub leads to
The second intake valve is crossed to be connected with air inlet pipeline；The outlet of first tub passes through the first air outlet valve and the gas outlet pipeline
Connection, the outlet of second tub is connected by the second air outlet valve with the gas outlet pipeline；
The regeneration module includes air intake, air outlet slit, heater, cooler and air blower, the air intake
Be connected with the first end of tee pipe fitting, the second end pipe road of the tee pipe fitting be sequentially connected the air blower, the first control valve,
The heater, the second control valve and the cooler, the three-terminal link of the cooler and the tee pipe fitting；
The heating exit of the heater is connected by the 3rd control valve with the export pipeline of first tub, described to add
The heating exit of hot device is connected by the 4th control valve with the export pipeline of second tub；
The branch road of air outlet one of the air blower is connected with first control valve, and another branch road is connected by the 5th control valve
First mouth of pipe of four-way pipe fitting is connect, second mouth of pipe of the four-way pipe fitting passes through the entrance of the 6th control valve and first tub
Pipeline is connected, and the 3rd mouth of pipe of the four-way pipe fitting is connected by the 7th control valve with the entrance pipe of second tub, institute
The 4th mouth of pipe for stating four-way pipe fitting is connected by the 8th control valve with the air outlet slit.
Optionally, first tub and the built-in filter for being equipped with splendid attire adsorbent of second tub, the filter will
The inside division of first tub and second tub is heart and outer shroud two parts, and the adsorbent includes the first particle diameter
Aluminum oxide and the second particle diameter aluminum oxide, first particle diameter are more than the second particle diameter, and the inner parts contain second particle diameter
Aluminum oxide, the outer ring portion contain the first particle diameter aluminum oxide.
Optionally, the adsorbent also includes molecular sieve, and the first particle diameter aluminum oxide and the second particle diameter aluminum oxide contain
The bottom of the close entrance inside first tub and second tub；The molecular sieve is contained in described first
The top of the close outlet inside tub and second tub.
Optionally, air exhauster is set in the air outlet slit, the air outlet slit is connected with the air exhauster interface.
Optionally, the entrance of first tub and the entrance and exit of second tub are all connected with stainless steel air point
Device is flowed, the current divider is toroidal, and multiple stomatas are evenly distributed with the annulus body.
Optionally, the entrance of first tub and the entrance and exit of second tub are all connected with stainless steel air point
Device is flowed, the current divider is gondola water faucet shape, and multiple stomatas are evenly distributed with the gondola water faucet body.
Optionally, multiple stomatas are evenly distributed with the gondola water faucet body, each stomata is connected with time isocon, institute
The tube wall for stating time isocon is evenly equipped with multiple tap holes of different directions.
The utility model additionally provides a kind of energy-efficient drying system of absorption type, including such as any institutes of claim 1- 7
State the energy-efficient drying device of absorption type and three-stage filtration component, the outlet of the air compressor machine and entering for the three-stage filtration component
Mouth connection, the outlet of the three-stage filtration component is connected with the air inlet.
Optionally, the three-stage filtration component includes moisture trap, accurate filter and the ultraprecise mistake being sequentially connected in series
Filter, the outlet of the air compressor machine are connected with the entrance of the moisture trap, the outlet of the ultraprecise filter with it is described
Air inlet connects.
Optionally, in addition to rearmounted dust removal filter, the entrance of the rearmounted dust removal filter are connected with the gas outlet.
Relative to prior art, the energy-efficient drying device course of work of absorption type provided by the utility model includes inhaling
Attached, thermal regeneration, circulating cooling, standby, absorption circulation technology, first barrel of tub and the second tub are replaced by adsorbing pipeline
Execution is adsorbed by drying technique, then by regeneration module, completes blast heating regeneration, the process of sealing and circulating cooling, and realizes the
The recycling of one tub and the second tub.Whole flow process not consumption of compressed air, compressed air quality is high, reduces power consumption,
Energy-saving effect is obvious.
Further, designed by optimizing the decker of adsorbent, optimize flow direction and the speed of air-flow, enter one
Step improves the quality of compressed air.
The utility model additionally provides the energy-efficient drying system of absorption type, due to high system that employs above-mentioned absorption type
Energy-saving drying device is imitated, therefore there is identical beneficial effect.
Brief description of the drawings
Accompanying drawing is to be further understood for providing to of the present utility model, and a part for constitution instruction, and following
Embodiment be used to explain the utility model together, but do not form to limitation of the present utility model.
Fig. 1 is the schematic diagram of the energy-efficient drying device of absorption type provided by the utility model；
Fig. 2 is the schematic diagram of the energy-efficient drying system of absorption type provided by the utility model.
Wherein, the corresponding relation between the reference in Fig. 1 and Fig. 2 and component names is as follows：
1 air compressor machine,
The energy-efficient drying device of 2 absorption types,
21 air inlets,
22 gas outlets,
23 first tubs,
24 second tubs,
25 regeneration modules,
31 first intake valves,
32 second intake valves,
33 first air outlet valves,
34 second air outlet valves,
251 air intakes,
252 air outlet slits,
253 heaters,
254 coolers,
255 air blowers,
41 first control valves,
42 second control valves,
43 the 3rd control valves,
44 the 4th control valves,
45 the 5th control valves,
46 the 6th control valves,
47 the 7th control valves,
48 the 8th control valves,
5 three-stage filtration components,
51 moisture traps,
52 accurate filters,
53 ultraprecise filters,
6 rearmounted dust removal filters.
Embodiment
In order that those skilled in the art more fully understand the utility model, below in conjunction with the accompanying drawings and it is embodied
The utility model is described in further detail for mode.
Fig. 1 and Fig. 2 are refer to, Fig. 1 is the schematic diagram of the energy-efficient drying device of absorption type provided by the utility model；Figure
2 be the schematic diagram of the energy-efficient drying system of absorption type provided by the utility model.
In a kind of specific embodiment, a kind of energy-efficient drying device of absorption type provided by the utility model, bag
Air inlet 21 and gas outlet 22 are included, air inlet 21 is connected with the outlet of air compressor machine 1；
The energy-efficient drying device of absorption type also includes the first tub 23, the second tub 24 and regeneration module 25；
The entrance of first tub 23 is connected by the first intake valve 31 with the pipeline of air inlet 21, and the entrance of the second tub 24 leads to
The second intake valve 32 is crossed to be connected with the pipeline of air inlet 21；Managed by the first air outlet valve 33 with gas outlet 22 outlet of first tub 23
Road is connected, and the outlet of the second tub 24 is connected by the second air outlet valve 34 with the pipeline of gas outlet 22；
Regeneration module 25 includes air intake 251, air outlet slit 252, heater 253, cooler 254 and air blower 255,
Air intake 251 is connected with the first end of tee pipe fitting, and the second end pipe road of tee pipe fitting is sequentially connected air blower 255, first
Control valve 41, heater 253, the second control valve 42 and cooler 254, the three-terminal link of cooler 254 and tee pipe fitting；
The heating exit of heater 253 is connected by the 3rd control valve 43 with the export pipeline of the first tub 23, heater
253 heating exit is connected by the 4th control valve 44 with the export pipeline of the second tub 24；
The branch road of air outlet one of air blower 255 is connected with the first control valve 41, and another branch road is connected by the 5th control valve 45
Connect first mouth of pipe of four-way pipe fitting, the entrance pipe that second mouth of pipe of four-way pipe fitting passes through the 6th control valve 46 and the first tub 23
Connection, the 3rd mouth of pipe of four-way pipe fitting are connected by the 7th control valve 47 with the entrance pipe of the second tub 24, four-way pipe fitting
4th mouth of pipe is connected by the 8th control valve 48 with air outlet slit 252.
Relative to prior art, the energy-efficient drying device course of work of absorption type provided by the utility model includes inhaling
Attached, thermal regeneration, circulating cooling, standby, absorption circulation technology, first barrel of tub and the second tub 24 are handed over by adsorbing pipeline
Technique is adsorbed by drying for execution, then is regenerated by regeneration module 25, completion blast heating, the process of sealing and circulating cooling, and it is real
The recycling of existing first tub 23 and the second tub 24.Whole flow process not consumption of compressed air, compressed air quality is high, reduces
Power consumption, energy-saving effect are obvious.
The operation principle of the absorption drier of continuous firing is Dynamic Adsorption principle.This refers to needing dry compression
Air enters desiccant layer, and then the moisture in air is absorbed.Because the drying capacity of drier is limited, full reaching
Before, will change.With the transformation of drier tub operation principle, point of use can endlessly obtain dry
Compressed air.
The course of work of the energy-efficient drying device of absorption type includes：
Stroke is adsorbed, absorption stroke is by the bottom up operation of tub.
Specifically, the contracting air of vapour pressure containing saturation of the discharge of air compressor machine 1 is via being installed on the first of the bottom of the first tub 23
Intake valve 31, into the first tub 23, saturation aqueous vapor is may insure using various stainless steel air diverter in the first tub 23
Compressed air can flow through sorbing material in all tubs, while its Water Molecular Adsorption carried is in drier.And reach institute's palpus
The drying compressed air of dew point is then by the top of the first tub 23, via the import system of the first air outlet valve 33.
Stroke is regenerated, it is to use to be flowed to by tub top down to transport to flow to reverse thermal regeneration stroke with absorption stroke
OK.
Specifically, while compressed air is dried through the first tub 23, the second tub 24 that moisture reaches saturation starts
Carry out regenerative process.Before reproducer starts, the pressure in the second tub 24 will slowly decline, until atmospheric pressure.This
Drying device in utility model carries out regeneration treatment using atmospheric air.Regenerative blower 255 by air be sent to below plus
In hot device 253, air is heated to required regeneration temperature, the rising of the air themperature of blower fan blowout is to heater 253
Power demand has active influence.
The air of air blower 255 is carried out at regeneration by the first control valve 41 and the 6th control valve 46 into the second tub 24
Reason.The moisture adsorbed will evaporate to be discharged into air then as air-flow from the 4th control valve 44 and the 8th control valve 48.
The regenerative process is carried out by back draught, and in this way, moisture is with prestissimo slave unit air inlet.
Under the evaporation of moisture, the air being heated will be cooled down when flowing through the second tub 24, Suo Youzai
It is so high that temperature during raw air discharge is far from evaporating temperature（About 40-60 °C）.As regenerative process is carried out, moisture
The reduction of content, the temperature of regeneration air will rise.After required temperature is reached, regenerative process will stop.
Stroke is cooled down, cooling stroke airflow direction is identical with absorption stroke directions, from the bottom up operation of tub, cooling row
Journey is closed loop.
To avoid temperature and dew point after changing from reaching highest, the heat stored in drier（After regeneration）Will be cooled
Air draught is taken away.The direction of cooling air-flow is as adsorption process, from top to bottom.It can prevent from doing by using this method
Drying prescription overloads, and improves dry mass.The air that the air blower 255 of drying device 2 of the present utility model sucks is in closed-loop path
Flowing, it can be ensured that cooling procedure is with environmental condition without any association.
Cooling stroke starts, the inverted running of air blower 255.Cooling system of the air that now air blower 255 is blown into closure
System flows in loop, and the cooling water of the cooled device 254 of heat is taken away.
After the completion of cooling program, the second tub 24 will be slowly pressurized.Once pressure is consistent with system pressure, will enter
Alternate program.
Two tub alternating sorbents, regeneration, the circulation of cooling more than, realize that endlessly product supplies.
Preferably, the first tub 23 and the second tub 24 is built-in is equipped with the filter for containing adsorbent, filter is by the first tub
23 and second the inside division of tub 24 be heart and outer shroud two parts, adsorbent includes the first particle diameter aluminum oxide and the second particle diameter
Aluminum oxide, the first particle diameter are more than the second particle diameter, and inner parts contain the second particle diameter aluminum oxide, and outer ring portion contains the first particle diameter oxygen
Change aluminium.
Designed by the decker for optimizing adsorbent, the adsorbent of small particle is contained in inner parts, makes script flow velocity
Faster central part flow slowing down absorption, outer ring portion contain the adsorbent of greater particle size, the slower outer shroud air-flow of script flow velocity
Accelerate absorption, this layout optimises the flow direction of air-flow and speed, further increase the quality of compressed air.
In addition, adsorbent also includes molecular sieve, the first particle diameter aluminum oxide and the second particle diameter aluminum oxide are contained in the first tub
23 and the bottom of the second close entrance inside tub 24；Molecular sieve is contained in leaning on inside the first tub 23 and the second tub 24
The top closely exported.Adsorption process is further optimized, first oxidized aluminium adsorbent adsorbs to realize, is inhaled by molecular sieve depth
Attached flow, further increases product quality.
In order to further optimize the flow of adsorbent reactivation, air outlet slit 252 set air exhauster, air outlet slit 252 with
Air exhauster interface connects.The setting of air exhauster can accelerate regeneration gas air flow, shorten air and flowed in the pipeline of same length
The dynamic time, energy dissipation is reduced, improve regeneration efficiency.
Current dryer is due to the design problem generally existing channeling of tub, i.e. in system, because gas is uneven
Even flowing, fluid open the passage of a resistance very little, form ditch, and gas passes through bed, shadow with the extremely short residence time
Ring adsorption effect.In another specific embodiment, the entrance and exit of the entrance of the first tub 23 and the second tub 24 is equal
Stainless steel air diverter is connected, current divider is toroidal, and multiple stomatas are evenly distributed with annulus body.Toroidal can
The inlet gas uniform divided flows of tub will be entered, be that air-flow can be even by the adsorbent in tub, improve product quality.
Current divider can also be gondola water faucet shape, and multiple stomatas are evenly distributed with gondola water faucet body.Preferably, on gondola water faucet body
Multiple stomatas are evenly distributed with, each stomata is connected with time isocon, and the tube wall of secondary isocon is evenly equipped with the multiple of different directions
Tap hole.The shunting flow direction of gas is further optimized, so that gas more uniformly sufficiently flows through adsorbent, is further carried
High adsorption efficiency, improve product quality.
It should be noted that all valves in the utility model can use globe valve, magnetic valve, pneumatic operated valve etc., with reality
Now to the folding of pipeline for the purpose of.
Cooler 254 in the utility model can use circulating water mode.Closed cooling will not introduce impurity, cooling
Effect is good.
Heater 253 in the utility model can use the mode such as electrical heating or steam heating to realize, especially, above-mentioned to add
The heat exchanger plates of hot device 253 use graphene board or graphene clad plate, can effectively increase heat exchange efficiency, and then improve revival
Rate.
In addition, the utility model additionally provides a kind of energy-efficient drying system of absorption type, including above-mentioned absorption type is efficient
Energy-saving drying device and three-stage filtration component 5, the outlet of air compressor machine 1 are connected with the entrance of three-stage filtration component 5, three-stage filtration group
The outlet of part 5 is connected with air inlet 21.Due to system that employs the energy-efficient drying device of above-mentioned absorption type, therefore there is phase
With beneficial effect, in addition, three-stage filtration component 5 be arranged on drying device before, compressed air is first passed through filtering, mistake
A large amount of steam and impurity therein are filtered, reduces the adsorption strength of follow-up drying device, adds the service life of drying device,
Operating cost is reduced, improves the operating efficiency of system.
Preferably, three-stage filtration component 5 includes moisture trap 51, accurate filter 52 and the ultraprecise mistake being sequentially connected in series
Filter 53, the outlet of air compressor machine 1 are connected with the entrance of moisture trap 51, and outlet and the air inlet 21 of ultraprecise filter 53 connect
Connect.The minute impurities and suspended particulates that ultraclean filters can be filtered out further, further reduce the absorption of follow-up drying device
Intensity, the service life of drying device is added, improve the operating efficiency of system, improve product quality.
Preferably, drying system also includes rearmounted dust removal filter 6, the entrance of rearmounted dust removal filter 6 and gas outlet
22 connections, the rearmounted dust removal filter 6 can filter the impurity such as the powder carried in the gas after absorption, improve product degree of purity.
Detailed Jie has been carried out to a kind of energy-efficient drying device of absorption type provided by the utility model and system above
Continue.Specific case used herein is set forth to principle of the present utility model and embodiment, and above example is said
It is bright to be only intended to help and understand method and its core concept of the present utility model.It should be pointed out that for the common of the art
For technical staff, on the premise of the utility model principle is not departed from, can also to the utility model carry out it is some improvement and
Modification, these are improved and modification is also fallen into the protection domain of the utility model claims.
Claims (10)
1. a kind of energy-efficient drying device of absorption type, it is characterised in that including air inlet（21）And gas outlet（22）, it is described enter
Gas port（21）With air compressor machine（1）Outlet connection；
The energy-efficient drying device of absorption type also includes the first tub（23）, the second tub（24）And regeneration module（25）；
First tub（23）Entrance pass through the first intake valve（31）With the air inlet（21）Pipeline connects, and described second
Tub（24）Entrance pass through the second intake valve（32）With the air inlet（21）Pipeline connects；First tub（23）Go out
Mouth passes through the first air outlet valve（33）With the gas outlet（22）Pipeline connects, second tub（24）Outlet go out by second
Air valve（34）With the gas outlet（22）Pipeline connects；
The regeneration module（25）Including air intake（251）, air outlet slit（252）, heater（253）, cooler（254）With
Air blower（255）, the air intake（251）It is connected with the first end of tee pipe fitting, the second end pipe road of the tee pipe fitting
It is sequentially connected the air blower（255）, the first control valve（41）, the heater（253）, the second control valve（42）It is and described
Cooler（254）, the cooler（254）With the three-terminal link of the tee pipe fitting；
The heater（253）Heating exit pass through the 3rd control valve（43）With first tub（23）Export pipeline connect
Connect, the heater（253）Heating exit pass through the 4th control valve（44）With second tub（24）Export pipeline connect
Connect；
The air blower（255）The branch road of air outlet one and first control valve（41）Connection, another branch road pass through the 5th control
Valve processed（45）First mouth of pipe of four-way pipe fitting is connected, second mouth of pipe of the four-way pipe fitting passes through the 6th control valve（46）With it is described
First tub（23）Entrance pipe connection, the 3rd mouth of pipe of the four-way pipe fitting passes through the 7th control valve（47）With described second
Tub（24）Entrance pipe connection, the 4th mouth of pipe of the four-way pipe fitting passes through the 8th control valve（48）With the air outlet slit
（252）Connection.
2. the energy-efficient drying device of absorption type as claimed in claim 1, it is characterised in that first tub（23）And institute
State the second tub（24）Built-in to be equipped with the filter for containing adsorbent, the filter is by first tub（23）With described second barrel
Groove（24）Inside division be heart and outer shroud two parts, the adsorbent includes the first particle diameter aluminum oxide and the second particle diameter aoxidizes
Aluminium, first particle diameter are more than the second particle diameter, and the inner parts contain the second particle diameter aluminum oxide, and the outer ring portion is contained
Fill the first particle diameter aluminum oxide.
3. the energy-efficient drying device of absorption type as claimed in claim 2, it is characterised in that the adsorbent also includes molecule
Sieve, the first particle diameter aluminum oxide and the second particle diameter aluminum oxide are contained in first tub（23）With second tub（24）
The bottom of the internal close entrance；The molecular sieve is contained in first tub（23）With second tub（24）It is interior
The top of the close outlet in portion.
4. the energy-efficient drying device of absorption type as claimed in claim 3, it is characterised in that in the air outlet slit（252）
Air exhauster, the air outlet slit are set（252）It is connected with the air exhauster interface.
5. the energy-efficient drying device of absorption type as described in claim 1-4 is any, it is characterised in that first tub
（23）Entrance and second tub（24）Entrance and exit be all connected with stainless steel air diverter, the current divider is circle
Ring-shaped, multiple stomatas are evenly distributed with the annulus body.
6. the energy-efficient drying device of absorption type as described in claim 1-4 is any, it is characterised in that first tub
（23）Entrance and second tub（24）Entrance and exit be all connected with stainless steel air diverter, the current divider is flower
Shape is spilt, multiple stomatas are evenly distributed with the gondola water faucet body.
7. the energy-efficient drying device of absorption type as claimed in claim 6, it is characterised in that uniformly divide on the gondola water faucet body
Multiple stomatas are furnished with, each stomata is connected with time isocon, and the tube wall of the secondary isocon is evenly equipped with the more of different directions
Individual tap hole.
8. a kind of energy-efficient drying system of absorption type, it is characterised in that including the absorption type as described in claim 1- 7 is any
Energy-efficient drying device and three-stage filtration component（5）, the air compressor machine（1）Outlet and the three-stage filtration component（5）'s
Entrance connects, the three-stage filtration component（5）Outlet and the air inlet（21）Connection.
9. the energy-efficient drying system of absorption type as claimed in claim 8, it is characterised in that the three-stage filtration component（5）
Including the moisture trap being sequentially connected in series（51）, accurate filter（52）With ultraprecise filter（53）, the air compressor machine（1）'s
Outlet and the moisture trap（51）Entrance connection, the ultraprecise filter（53）Outlet and the air inlet（21）
Connection.
10. the energy-efficient drying system of absorption type as claimed in claim 9, it is characterised in that also including rearmounted dust removal and filtration
Device（6）, the rearmounted dust removal filter（6）Entrance and the gas outlet（22）Connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720855988.9U CN207012777U (en) | 2017-07-14 | 2017-07-14 | A kind of energy-efficient drying device of absorption type and system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720855988.9U CN207012777U (en) | 2017-07-14 | 2017-07-14 | A kind of energy-efficient drying device of absorption type and system |
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| Publication Number | Publication Date |
|---|---|
| CN207012777U true CN207012777U (en) | 2018-02-16 |
Family
ID=61484586
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720855988.9U Expired - Fee Related CN207012777U (en) | 2017-07-14 | 2017-07-14 | A kind of energy-efficient drying device of absorption type and system |
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| Country | Link |
|---|---|
| CN (1) | CN207012777U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107213760A (en) * | 2017-07-14 | 2017-09-29 | 湖南和鑫新能源技术有限公司 | A kind of energy-efficient drying device of absorption type and system |
| CN111054191A (en) * | 2019-12-31 | 2020-04-24 | 攀钢集团西昌钢钒有限公司 | Compressed air drying device and compressed air supply system |
-
2017
- 2017-07-14 CN CN201720855988.9U patent/CN207012777U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107213760A (en) * | 2017-07-14 | 2017-09-29 | 湖南和鑫新能源技术有限公司 | A kind of energy-efficient drying device of absorption type and system |
| CN111054191A (en) * | 2019-12-31 | 2020-04-24 | 攀钢集团西昌钢钒有限公司 | Compressed air drying device and compressed air supply system |
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Granted publication date: 20180216 |