CN204865472U - Compressed air drying adsorption tower - Google Patents
Compressed air drying adsorption tower Download PDFInfo
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- CN204865472U CN204865472U CN201520639766.4U CN201520639766U CN204865472U CN 204865472 U CN204865472 U CN 204865472U CN 201520639766 U CN201520639766 U CN 201520639766U CN 204865472 U CN204865472 U CN 204865472U
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- compressed air
- adsorption tower
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Abstract
The utility model relates to a compressed air drying adsorption tower is refered in particular to in the gas drying field, including adsorbing tower body, adsorbent, heat exchanger, the adsorbent is filled in the adsorption tower internally, the heat exchanger sets up among the adsorbent with the mode of displaceable, and the inner space of heat exchanger does not communicate with each other with the inner space that adsorbs the tower body is isolated, and the heat transfer pipeline of heat exchanger passes the shell that adsorbs the tower body. After adopting above -mentioned scheme, can be more high -efficient, the energy consumption is lower carries out drying process to compressed air.
Description
Technical field
The utility model relates to the dry field of gas, refers in particular to a kind of compressed air drying adsorption tower.
Background technology
Compressed air is applied in large quantities in many industries, in order to obtain dry compressed air, needs to process the compressed air of air compressor machine output, the moisture in removing compressed air.The drying equipment be widely used at present has absorption drier and freezing type drier.The water removal effect of absorption drier is good, but observable index is higher, and freezing type drier observable index is lower, but water removal effect is poor.
The compressed air adsorption tower of prior art is the adsorbent (molecular sieve, activated alumina, silica gel etc.) of filling some in a container, moisture compressed air enters from one end of container, pass through adsorbent, moisture in compressed air is by adsorbent, thus obtaining dry compressed air, dry compressed air is from the other end output of container.Ability due to the adsorption moisture of adsorbent is limited, and when after the moisture that absorption is abundant, its adsorption capacity can decline, and does not even adsorb, and at this moment will carry out regeneration processed to adsorbent, and the regeneration of adsorbent can be heatless regeneration and have hot recycling.During the moisture of adsorbent in adsorption compression air, can discharge a large amount of heats (heat of condensation), adsorbent, when regenerating dehydration, absorb a large amount of heats (heat of vaporization).Particularly when adsorption tower dehydration regeneration, regeneration air is from entrance to outlet, and the heat of vaporization in time dewatering with the heat exchange and supplementary adsorbent of adsorbent, temperature promptly reduces.The temperature of regeneration air directly determines the ability that regeneration air receives steam, and regeneration air temperature is high, and the steam vapour amount that can receive is just many, and regeneration air amount just can correspondingly reduce.The adsorption tower of prior art is owing to only relying on regeneration air to carry heat, and by regeneration air quantitative limitation, promptly the temperature of regeneration air can not be improved (temperature that can reduce regeneration air during heatless regeneration), the steam that receives of regeneration air is few in a long time, cause regeneration air consumption to increase, energy consumption increases.Therefore, the present inventor makes further research this, and develop a kind of compressed air drier, this case produces thus.
Utility model content
The purpose of this utility model is to provide a kind of compressed air drying adsorption tower, can lower the carrying out drying to compressed air and process of more efficient, energy consumption.
To achieve these goals, the technical solution of the utility model is as follows:
A kind of compressed air drying adsorption tower, comprise absorption tower body, adsorbent, heat exchanger, described adsorbent is filled in absorption tower body, described heat exchanger is arranged among adsorbent in replaceable mode, the inner space of heat exchanger does not communicate with the inner space of absorption tower body is isolated, and the heat exchange pipeline of heat exchanger passes the shell of absorption tower body.
Further, the two ends up and down of described absorption tower body are offered and are respectively had compressed air mouth; The opening of described heat exchanger tube connector is heat exchange air port, and described heat exchange air port is opened in the upper and lower two ends of absorption tower body shell.
Further, in described absorption tower body inside, screen pack is housed, described screen pack is positioned at inside compressed air mouth, and described heat exchanger is coil arrangement or the multilayer straight tube structure of multilayer.
Further, a kind of drying device comprising above-mentioned compressed air drying adsorption tower, comprise adsorption tower A, adsorption tower B, aerial cooler, described adsorption tower A and adsorption tower B is arranged in parallel, and described aerial cooler is communicated with adsorption tower B with adsorption tower A by some valves.
After adopting such scheme, the utility model compared with prior art, has the following advantages:
By the heat exchanger in adsorption tower internal placement, by the heat transfer type of the conduction and convection of heat, carry out heat exchange with adsorbent, reach in time, carry out efficiently the effect of heat exchange; Both promptly can heat adsorbent, and can also cool adsorbent efficiently, make drying effect good, energy consumption is low.
Accompanying drawing explanation
Fig. 1 is prior art adsorption tower structure chart;
Fig. 2 is the structure chart of the utility model adsorption tower;
Fig. 3 is a kind of adsorption tower according to principle design of the present utility model;
Fig. 4 is Fig. 3 top view;
Fig. 5 is the sectional view of Fig. 3
Fig. 6 is the flow chart of a kind of zero gas consumption compressed air drier according to the utility model design.
Fig. 7 adsorbs according to the adsorption tower A of a kind of zero gas consumption compressed air drier of the utility model design, flow chart when adsorption tower B regenerates
Fig. 8 adsorbs according to the adsorption tower A of a kind of zero gas consumption compressed air drier of the utility model design, flow chart during adsorption tower B blast-cold
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is further described.
Fig. 1 is the structure chart of prior art adsorption tower, and there is compressed air mouth (01,02) at absorption tower body (03) two ends, and absorption tower body (03) inside is full of adsorbent (04).In order to prevent adsorbent (04) from running out of, screen pack (05,06) is housed in absorption tower body (03) inside.The working method of drying tower is divided into adsorption process and regenerative process.Adsorption process: compressed air enters from compressed air mouth (01), by adsorbent (104) by the water adsorption in compressed air in adsorbent (04), dry compressed air goes out (02) output from compressed air.Regenerative process: regeneration air enters from compressed air mouth (02), is departed from moisture wherein by adsorbent (04), and the air of band water is disposed to air from compressed air mouth (01).During the moisture of adsorbent in adsorption compression air, can discharge a large amount of heats (heat of condensation), adsorbent, when regenerating dehydration, absorb a large amount of heats (heat of vaporization).Particularly when adsorption tower dehydration regeneration, regeneration air enters to compressed air mouth (01) from compressed air mouth (02) and discharges, while regeneration air receives moisture, by carrying out when supplementary adsorbent dewaters heat of vaporization with the heat exchange of adsorbent (04), temperature promptly reduces.The temperature of regeneration tail gas directly determines the ability that regeneration air receives steam, and regeneration tail gas temperature is high, and the steam vapour amount that can receive is just many, and regeneration air amount just can correspondingly reduce.The adsorption tower of prior art is owing to only relying on regeneration air to carry heat, and by regeneration air quantitative limitation, promptly the temperature of regeneration tail gas can not be improved (temperature that can reduce regeneration tail gas during heatless regeneration), the steam that receives of regeneration air is few in a long time, cause regeneration air consumption to increase, energy consumption increases.In absorption tower adsorbs process, compressed air enters to compressed air mouth (02) output from compressed air mouth (01), when moisture in compressed air is adsorbed, releases heat (heat of condensation), these heat parts are taken away by compressed air, remaining heat accumulation is inner at adsorption tower, makes the temperature of adsorbent (04) increase.After adsorbent (04) heats up, adsorption efficiency declines, and can only terminate adsorption process in advance and regenerate, reduce the adsorption efficiency of adsorbent (04).
Compressed-air actuated drying means of the present utility model and adsorption tower can not discharge the heat of condensation in time for prior art adsorption tower exactly, the improvement that the problem of supplementing heat of vaporization is made.Below be described in detail.
Adsorption tower of the present utility model comprises compressed air mouth (101,102), absorption tower body (103), adsorbent (104), screen pack (105,106), heat exchanger (107), heat exchange air port (108,109), heat exchanger tube connector (110) composition.
There is compressed air mouth (101,102) at absorption tower body (103) two ends, and absorption tower body (103) inside is full of adsorbent (104).In order to prevent adsorbent (104) from running out of, screen pack (105,106) is housed in absorption tower body (103) inside.Place a heat exchanger (107), the outer surface of heat exchanger and adsorbent contact in absorption tower body (103) inside, inner completely cutting off with outer surface does not communicate, and heat exchanger can be the form such as the coil pipe of multilayer or the straight tube of multilayer.Heat exchanger passes the outer wall of absorption tower body (103) by tube connector (110), and two ends arrange heat exchange air port (108,109).
The operation principle of adsorption tower of the present utility model is divided into adsorption process, regenerative process and blast-cold process.
Adsorption process: compressed air enters from compressed air mouth (101), successively by adsorbent (104) and heat exchanger (107).When compressed air is by adsorbent (104), adsorbent (104) by the water adsorption in compressed air in adsorbent (104), the heat of condensation heated compressed air discharged during absorption makes it heat up, when the compressed air heated up is by heat exchanger (107), heat is passed to the heat transferring medium passed through in heat exchanger (107), compressed-air actuated temperature declines.So adsorb-heat up-cooling-cooling repeatedly, dry compressed air is from compressed air mouth (102) output, and the heat of condensation is also taken away by the heat transferring medium passed through in parallel operation (107), solves the problem of temperature rise of adsorbent (104).Heat transferring medium (being the air by environment temperature here) enters from heat exchange air port (109), by heat exchanger tube connector to heat exchanger (107), discharges, the heat produced in adsorption process is taken away after absorption heat from heat exchange air port (108).
Regenerative process: regeneration air enters from compressed air mouth (102), successively by adsorbent (104) and heat exchanger (107).When regeneration air is by adsorbent (104), the moisture in adsorbent (104) is evaporated in regeneration air, absorbs heat of vaporization, the temperature of regeneration air is declined during moisture evaporation from regeneration air.When the regeneration air of cooling is by heat exchanger (107), the heat of the high temperature heat transferring medium passed through in absorption heat-exchange device (107), the temperature of regeneration air rises.So regenerate repeatedly-cooling-heating-heat up, moisture regeneration air is discharged from compressed air mouth (101), and heat transferring medium constantly by heat exchanger (107) additional heat, solves the cooling problem of adsorbent (104).The heat transferring medium of high temperature enters from heat exchange air port (109), by heat exchanger tube connector to heat exchanger (107), discharge after heating adsorption agent and regeneration air from heat exchange air port (108), for regenerative process additional heat, adsorbent is heated to high temperature.
Blast-cold process: when adopting dry air to carry out blast-cold, blowing cold air enters from compressed air mouth (102), and discharge to compressed air mouth (101), heat transferring medium is surrounding air, is cooled adsorbent (104) by heat exchanger.When adopting wet (moisture) compressed air to carry out blast-cold, blowing cold air enters from compressed air mouth (101), and discharge to compressed air mouth (102), heat transferring medium is surrounding air, is cooled adsorbent (104) by heat exchanger (107).
Fig. 3 is a kind of adsorption tower according to the utility model principle design, is made up of adsorption tower shell (201), heat exchanger (202), compressed air mouth (203), compressed air mouth (204), heat exchanger supervisor (205,206,207,208), heat exchanger arm (209,210,211,212), heat exchanger tube (213,214).Adsorption tower shell (201) inside is full of adsorbent (molecular sieve, activated alumina, silica gel etc.), and compressed air enters adsorption tower inside from compressed air mouth (203), and dry compressed air is discharged from compressed air mouth (204).
Heat exchanger supervisor (205, 206, 207, 208) upper respectively from adsorption tower shell (201), lower end passes, heat exchanger supervisor (206) is connected with heat exchanger arm (209), heat exchanger arm (209) and heat exchanger tube (213) are connected, heat exchanger tube (213) is connected with heat exchanger arm (210), heat exchanger arm (210) is responsible for (206) and is connected with heat exchanger, heat transferring medium enters from heat exchanger supervisor (205), by heat exchanger arm (209), by heat exchanger tube (213), by heat exchanger arm (210), by heat exchanger supervisor (206), discharge from heat exchanger supervisor (206), complete heating and cooling process.Heat exchanger supervisor (207) is connected with heat exchanger arm (211), heat exchanger arm (211) is connected with heat exchanger tube (214), heat exchanger tube (214) is connected with heat exchanger arm (212), heat exchanger arm (212) is responsible for (208) and is connected with heat exchanger, heat transferring medium enters from heat exchanger supervisor (207), by heat exchanger arm (211), by heat exchanger tube (214), by heat exchanger arm (212), by heat exchanger supervisor (208), discharge from heat exchanger supervisor (208), complete heating and cooling process.
Fig. 6 is a kind of compressed air drier according to the utility model principle design, comprise compressed air mouth (301), compressed air mouth (302), adsorption tower A(303), adsorption tower B(304), aerial cooler (305, 306), centrifugal blower (308, 308), cyclelog (309), cooling air import (310, 312), cooling air outlet (311, 313), stop valve (401, 405, 406, 407, 408, 409, 413, 416, 417, 418, 419), check-valves (402, 403, 410, 411, 414, 415), stop valve (404, 412), ball valve (420, 421), admission pressure (P1), outlet pressure (P2), to give vent to anger dew point (LD), intake air temperature (T1), air outlet temperature (T2), one-level chilling temperature (T3), regeneration tail gas temperature (T4), secondary inlet temperature (T5), secondary chilling temperature (T6) is formed.
The compressed air of high temperature enters from compressed air mouth (301), and dry compressed air is from compressed air mouth (302) output.Cyclelog (309) sequential control valve temporally, the action of blower fan, make adsorption tower A(303), adsorption tower B(304) be alternately in adsorbed state, when an adsorption tower is in adsorbed state, another adsorption tower be then in regeneration or blast-cold state.
Adsorption tower A (303) adsorbs, adsorption tower B(304) flow process when regenerating is shown in Fig. 7.The compressed air of high temperature is introduced into adsorption tower B(304), the adsorbent of inside is heated and regenerates, after aerial cooler (305) cooling, enter adsorption tower A(303) removing moisture wherein, the compressed air of finished product is discharged from compressed air mouth (302).Ambient wind is after centrifugal blower (307) pressurization, by adsorption tower A(303), adsorbent and compressed air are cooled, discharge from cooling air outlet (312) after heat of condensation when taking away absorption, stop valve (412) is for bypass part high temperature compressed air, after aerial cooler (306) cooling, enter adsorption tower A(303) process, object is reduced by adsorption tower B(304) high temperature compressed air amount, reduce the resistance of system.Ball valve (420,421) is for the cooled condensate water of discharges compressed air.
Adsorption tower A (303) adsorb, adsorption tower B(304) blast-cold time flow process see Fig. 8.The compressed air of high temperature is introduced into aerial cooler (305) cooling, enter adsorption tower B(304) adsorbent of inside is cooled, compressed air after intensification enters adsorption tower A(303 again after aerial cooler (305) cooling) removing moisture wherein, the compressed air of finished product is discharged from compressed air mouth (302).Ambient wind is after centrifugal blower (307) pressurization, by adsorption tower A(303), adsorbent and compressed air are cooled, discharge from cooling air outlet (312) after heat of condensation when taking away absorption, ambient wind is after centrifugal blower (308) pressurization, by adsorption tower B(304), adsorbent and compressed air are cooled, discharge from cooling air outlet (313) after taking away inner heat, stop valve (404) directly enters adsorption tower A(303 for bypass part compressed air) process, object is reduced by adsorption tower B(304) blast-cold air supply, the resistance of reduction system.
Adsorption tower B (304) adsorbs, adsorption tower A(303) flow process when regenerating and adsorption tower B (304) absorption, adsorption tower A(303) blast-cold time flow process identical with front principle.
The feature of this device is not consumption of compressed air, utilizes the heat exchanger being positioned over adsorption tower inside to cool adsorbent and compressed air, can improve the effect of cooling, take away heat of adsorption, ensure compressed-air actuated up to standard, there is energy consumption low, the feature that absorption property is good.
Claims (4)
1. a compressed air drying adsorption tower, it is characterized in that: comprise absorption tower body, adsorbent, heat exchanger, described adsorbent is filled in absorption tower body, described heat exchanger is arranged among adsorbent in replaceable mode, the inner space of heat exchanger does not communicate with the inner space of absorption tower body is isolated, and the heat exchange pipeline of heat exchanger passes the shell of absorption tower body.
2. a kind of compressed air drying adsorption tower according to claim 1, is characterized in that: the two ends up and down of described absorption tower body are offered respectively compressed air mouth; The opening of described heat exchanger tube connector is heat exchange air port, and described heat exchange air port is opened in the upper and lower two ends of absorption tower body shell.
3. a kind of compressed air drying adsorption tower according to claim 1, it is characterized in that: in described absorption tower body inside, screen pack is housed, described screen pack is positioned at inside compressed air mouth, and described heat exchanger is coil arrangement or the multilayer straight tube structure of multilayer.
4. one kind comprises the drying device of above-mentioned compressed air drying adsorption tower, it is characterized in that: comprise adsorption tower A, adsorption tower B, aerial cooler, described adsorption tower A and adsorption tower B is arranged in parallel, and described aerial cooler is communicated with adsorption tower B with adsorption tower A by some valves.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520639766.4U CN204865472U (en) | 2015-08-24 | 2015-08-24 | Compressed air drying adsorption tower |
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| CN201520639766.4U CN204865472U (en) | 2015-08-24 | 2015-08-24 | Compressed air drying adsorption tower |
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| CN204865472U true CN204865472U (en) | 2015-12-16 |
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| CN201520639766.4U Expired - Fee Related CN204865472U (en) | 2015-08-24 | 2015-08-24 | Compressed air drying adsorption tower |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105148689A (en) * | 2015-08-24 | 2015-12-16 | 王新建 | Adsorption tower for drying compressed air |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105148689A (en) * | 2015-08-24 | 2015-12-16 | 王新建 | Adsorption tower for drying compressed air |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151216 Termination date: 20200824 |
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| CF01 | Termination of patent right due to non-payment of annual fee |