CN107511036A - Heatless regeneration absorption drying equipment - Google Patents
Heatless regeneration absorption drying equipment Download PDFInfo
- Publication number
- CN107511036A CN107511036A CN201710919384.0A CN201710919384A CN107511036A CN 107511036 A CN107511036 A CN 107511036A CN 201710919384 A CN201710919384 A CN 201710919384A CN 107511036 A CN107511036 A CN 107511036A
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- drying
- drying towers
- towers
- air
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0454—Controlling adsorption
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
- B01D53/261—Drying gases or vapours by adsorption
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40083—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Drying Of Gases (AREA)
Abstract
The invention discloses a kind of heatless regeneration absorption drying equipment, including A drying towers and B drying towers arranged side by side, and the controller being arranged between two drying towers, the A drying towers are dried tower bottom with B and connected by an admission line；The discharge duct being connected in parallel with two air inlet Pneumatic valves and air intake is additionally provided with the admission line, exhaust outlet is provided with the middle part of the discharge duct, and the exhaust outlet is provided with silencer, on the discharge duct, exhaust outlet both sides be respectively provided with the exhaust a being electrically connected with the controller Pneumatic valve；The A drying towers are connected with the top of B drying towers by an outlet pipe, and the outlet pipe is provided with air outlet slit, and an outlet regulating valve is respectively provided between the air outlet slit pipe and A drying towers and B drying towers；Adsorbent is filled with the A drying towers and B drying towers.The design of drying equipment is reasonable, easy for installation, and drying effect is good, and drying efficiency is high, and regeneration gas consumption is few.
Description
Technical field
The present invention relates to a kind of drying equipment, and in particular to a kind of heatless regeneration absorption drying equipment.
Background technology
Heatless regeneration absorption drying equipment is to utilize principle of pressure swing adsorption, to remove the moisture content in compressed gas.At present
Dryer configuration be double-tower type, drying tower and regenerator alternate work, moved in circles, and reach drying purpose.Its work
Circulation is divided into absorption and two stages of regeneration：Drying stage, drying tower pressure rise, the steam partial pressure in air also accordingly carry
Height, when by drier bed, vapor is adsorbed by drier, gradually steps up desiccant surface steam partial pressure, reaches
Balance, makes compressed air obtain drying；Regeneration stage, tower inner air pressure is set to reduce suddenly, the partial pressure of vapor similarly drops
Low, the vapor adsorbed in drier is transferred in air, is desorbed drier.Adsorption process is that desiccant surface free energy subtracts
Few process, it does not need external enwergy to promote and the spontaneous progress of energy.Regenerative process is the inverse process of adsorption process, that is, drier
The process that surface free energy recovers, and regenerative process is the process of power consumption.Heatless regenerative adsorption dryer regenerative process follows 2
Individual principle：(1) principle is regenerated completely：Adsorb half period T in be adsorbed moisture, should certain time interval T ' in completely desorption side by side
Go out the outer (T' of tower<T), and desiccant temperature will reach the initial temperature of setting before next sorption cycle starts；(2) minimum consumption
Gas principle：Under certain regeneration pressure and discharge temperature, when regeneration tail gas water content is close to saturation, regeneration gas consumption is minimum.
If there is " meromorphosis " phenomenon in regeneration stage, desiccant surface activation recovering less than original level, influence by
The outlet dew point of compressed air is handled, while accumulation of the Residual water in drier can influence its service life.Therefore it is existing
Heatless regenerative adsorption dryer in order to avoid " meromorphosis ", increase regeneration gas consumption can meet the complete of drier as far as possible
Full regeneration, this results in the consumption of regeneration gas and the energy is excessive, but if reducing regeneration gas consumption, " meromorphosis " can be serious
Influence the service efficiency of drier and the service life of drier.
The content of the invention
The invention aims to solve above-mentioned technical problem, there is provided a kind of heatless regeneration absorption drying equipment, should
Design of drying equipment is reasonable, easy for installation, and drying effect is good, and drying efficiency is high, and regeneration gas consumption is few.
To achieve the above object, the technical solution adopted by the present invention is as follows：
A kind of heatless regeneration absorption drying equipment, including A drying towers and B drying towers arranged side by side, and it is arranged on two
Controller between drying tower, the A drying towers and B dry tower bottom and connected by an admission line, are set on the admission line
There is air intake, and the air inlet a being electrically connected with the controller gas is respectively provided between the air intake and A drying towers and B drying towers
Control valve；The discharge duct being connected in parallel with two air inlet Pneumatic valves and air intake, the row are additionally provided with the admission line
Be provided with exhaust outlet in the middle part of feed channel, and the exhaust outlet is provided with silencer, on the discharge duct, exhaust outlet both sides be respectively provided with one
The individual exhaust Pneumatic valve being electrically connected with the controller；The A drying towers are connected with the top of B drying towers by an outlet pipe, and this goes out
Feed channel is provided with air outlet slit, and an outlet regulation is respectively provided between the air outlet slit pipe and A drying towers and B drying towers
Valve；The air outlet slit is provided with air outlet slit pipe；Adsorbent is filled with the A drying towers and B drying towers.
Further, a horizontal stand is fixed with the middle part of the A drying towers and B drying towers, and controller is installed
On the horizontal stand.
Compared with prior art, the invention has the advantages that：
The drying equipment of the present invention reduces regeneration gas consumption while regeneration gas aridity is improved, and reduces energy waste
With the discharge of waste gas, while drying efficiency is improved, have reasonable in design, easy for installation, drying effect is good, and drying efficiency is high,
Regenerate the few advantage of gas consumption.
Brief description of the drawings
Fig. 1 is the process frame chart of the present invention.
Wherein, it is entitled corresponding to reference：
1-A drying towers, 2-B drying towers, 3- controllers, 4- admission lines, 5- air intakes, 6- air inlet Pneumatic valves, 7- rows
Feed channel, 8- exhaust outlets, 9- silencers, 10- exhaust Pneumatic valves, 11- outlet pipes, 12- air outlet slits, 13- outlet regulating valves,
14- air outlet slit pipes, 15- horizontal stands.
Embodiment
The invention will be further described with embodiment for explanation below in conjunction with the accompanying drawings, and mode of the invention includes but not only limited
In following examples.
The purpose of the present embodiment is to provide a kind of heatless regeneration absorption drying equipment, as shown in figure 1, the drying equipment bag
Include be set up in parallel and structure identical be filled with adsorbent A drying towers 1 and B drying towers 2, be arranged on A drying towers 1 and B done
The lower piping of the dry bottom of tower 2, and it is arranged on A drying towers 1 and the upper piping at the top of B drying towers 2；The A drying towers 1 and B are done
The dry middle part of tower 2 is also fixed with a horizontal stand 18, and the horizontal stand 18 is provided with controller 3.
The lower piping includes the admission line 4 for being arranged on A drying towers 1 and the bottom of B drying towers 2 and being connected, and this enters
Feed channel 4 is provided with air intake 5, and one and controller are respectively provided between the air intake and A drying towers 1 and B drying towers 2
The air inlet Pneumatic valve 6 of 3 electrical connections, is designated as Pneumatic valve A1 and Pneumatic valve B1 respectively；It is additionally provided with to enter with two on the admission line 4
The discharge duct 7 that gas Pneumatic valve 6 and air intake 5 are connected in parallel, the middle part of discharge duct 7 are provided with exhaust outlet 8, and the exhaust
Mouthfuls 8 are provided with the silencer 9 communicated with air, on the discharge duct 7, the both sides of exhaust outlet 8 be respectively provided with one and the electricity of controller 3
The exhaust Pneumatic valve 10 of connection, is designated as Pneumatic valve A2 and Pneumatic valve B2 respectively.
The upper piping includes being arranged on A drying towers 1 and the top of B drying towers 2 and the outlet pipe 11 connected, should
Outlet pipe 11 is provided with air outlet slit 12, and is respectively provided with one between the air outlet slit pipe and A drying towers 1 and B drying towers 2 and goes out
Gas regulating valve 13；The air outlet slit 12 is provided with air outlet slit pipe 14.
The operation principle of the present embodiment drying equipment is as follows：
This drying equipment utilizes pressure-variable adsorption regeneration cycle, makes compressed air exchange dry full of adsorbent through A, B two
When dry tower, i.e. a drying tower adsorb vapor under high partial pressures (operating pressure) state, another drying tower connects in low partial pressure
Parsed by air, then switched.Specific workflow is as follows：
Absorption：The following piping of humid air enters A drying towers through Pneumatic valve A1, bottom-up to flow through adsorbent layer, after drying
Air discharged from upper piping.
Regeneration：A small amount of dry air (about 10%) enters B drying towers, the drying after decompression by upper piping outlet regulating valve
Air (turning into regeneration gas) parses regeneration to the adsorbent in B drying towers from top to bottom, recovers the drying capacity of adsorbent, regeneration
It is discharged into after Pneumatic valve B2 and muffler that gas passes through lower piping in air.
Press：After adsorbent reactivation terminates, Pneumatic valve B2 is closed, and B drying towers gradually boost to the pressure that works online, accurately
Switching.
Switching：Lower piping Pneumatic valve B1 is opened, and Pneumatic valve A1 is closed, and Pneumatic valve A2 is opened, and the drying tower of A, B two is completed to cut
Change, B drying towers enter absorption, A drying towers release regeneration.
Above-described embodiment is only one of the preferred embodiment of the present invention, should not be taken to limit the protection model of the present invention
Enclose, as long as the present invention body design thought and that mentally makes have no the change of essential meaning or polishing, it is solved
Technical problem it is still consistent with the present invention, should be included in protection scope of the present invention within.
Claims (2)
1. a kind of heatless regeneration absorption drying equipment, including A drying towers (1) and B drying towers (2) arranged side by side, and be arranged on
Controller (3) between two drying towers, it is characterised in that the A drying towers (1) and B drying towers (2) bottom pass through an air inlet
Pipeline (4) connects, and the admission line is provided with air intake (5), and each between the air intake and A drying towers and B drying towers
Provided with an air inlet Pneumatic valve (6) electrically connected with controller (3)；It is additionally provided with the admission line (4) and two air inlet gas
The discharge duct (7) that control valve (6) and air intake (5) are connected in parallel, the discharge duct middle part are provided with exhaust outlet (8), and should
Exhaust outlet is provided with silencer (9), and on the discharge duct, exhaust outlet both sides are respectively provided with one and are electrically connected with controller (3)
It is vented Pneumatic valve (10)；Connected at the top of the A drying towers (1) and B drying towers (2) by an outlet pipe (11), the escape pipe
Road is provided with air outlet slit (12), and an outlet regulating valve is respectively provided between the air outlet slit pipe and A drying towers and B drying towers
(13)；The air outlet slit (12) is provided with air outlet slit pipe (14)；Filled in the A drying towers (1) and B drying towers (2)
There is adsorbent.
A kind of 2. micro-heat regeneration absorbent drying equipment according to claim 1, it is characterised in that the A drying towers (1)
A horizontal stand (15) is fixed with B drying towers (2) middle part, and controller (3) is arranged on the horizontal stand.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710919384.0A CN107511036A (en) | 2017-09-30 | 2017-09-30 | Heatless regeneration absorption drying equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710919384.0A CN107511036A (en) | 2017-09-30 | 2017-09-30 | Heatless regeneration absorption drying equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107511036A true CN107511036A (en) | 2017-12-26 |
Family
ID=60727124
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710919384.0A Withdrawn CN107511036A (en) | 2017-09-30 | 2017-09-30 | Heatless regeneration absorption drying equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107511036A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108905538A (en) * | 2018-09-30 | 2018-11-30 | 西安鑫顶天装备智能科技有限公司 | A kind of adsorption compressed air drier |
-
2017
- 2017-09-30 CN CN201710919384.0A patent/CN107511036A/en not_active Withdrawn
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108905538A (en) * | 2018-09-30 | 2018-11-30 | 西安鑫顶天装备智能科技有限公司 | A kind of adsorption compressed air drier |
| CN108905538B (en) * | 2018-09-30 | 2024-01-23 | 廊坊市顶天轻工机械有限公司 | Adsorption type compressed air dryer |
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| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20171226 |
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| WW01 | Invention patent application withdrawn after publication |