CN204710094U - Energy-efficient packed absorber - Google Patents
Energy-efficient packed absorber Download PDFInfo
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- CN204710094U CN204710094U CN201520402143.5U CN201520402143U CN204710094U CN 204710094 U CN204710094 U CN 204710094U CN 201520402143 U CN201520402143 U CN 201520402143U CN 204710094 U CN204710094 U CN 204710094U
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Abstract
The utility model discloses a kind of energy-efficient packed absorber, comprise tower body, be provided with gas in tower body upper end and go out pipe, tower body lower end is provided with leakage fluid dram, tower body top is provided with the first temperature-measuring port, first pressure tap, thin liquid inlet pipe and liquid distribution trough, liquid distribution trough is arranged on tower body inside and is connected with thin liquid inlet pipe, tower body lower outside wall is provided with the second temperature-measuring port, second pressure tap, gas inlet pipe and dope go out pipe, filler portion is provided with in tower body, described filler portion comprises packing layer, bed confinement plate and packing support plate, be positioned at gas and go out pipe bottom and be provided with demister in tower body.The utility model liquid distribution is even, distributed effect is good, the liquid water stream distributed can not be pooled in the middle part of liquid distribution trough, improves gas-liquid and exchanges effect, and can be separated at the mist produced after filler and the liquid phase be entrained in air-flow ascending air.
Description
Technical field
The utility model relates to a kind of gas-liquid switching equipment, especially energy-efficient packed absorber.
Background technology
Packed absorber is applicable to the absorption process of reacting fast and instantaneously, is used for gas cleaning, is a kind of equipment realizing absorption operation.What usual packed absorber adopted is counter-current operation, and absorbent adds with tower top and flows from top to bottom, and contact with the gas flowed from bottom to top, the liquid absorbing absorbent is discharged at the bottom of tower, and purified gas is discharged from tower top.Packed absorber can be used for resistant material and makes, and gas liquid interfacial area is large, and time of contact is long, the strong adaptability of tower during tolerance change, the advantage that tower resistance is little.
But, packed absorber liquid distribution effect is in the market bad, its liquid distribution head is fixed, and the liquid water stream of distribution is easily pooled in the middle part of liquid distribution trough and produces afflux, thus do not have the effect of distribution, and when the liquid of skewness flow in filler, the contact of liquids and gases can be reduced, thus affect gas-liquid exchange effect.
Simultaneously, because ascending air is in the liquid phase that can produce mist and be entrained in air-flow after filler, and these mists can affect the purity of giving vent to anger, therefore need to be separated the foam in ascending air and the liquid phase of carrying secretly, but the not easily separated mist compared with small particle diameter of demister of the interior installation of packed absorber at present, separative efficiency is not high, in addition, existing demister does not have liquid collecting function, the drop formed in foam removal process freely falls on the liquid distribution trough upper surface that is positioned at below demister by the impact that it is conducted oneself with dignity, can cause damage to liquid distribution trough after Long-Time Service is polluted to liquid distribution trough, affect the service life of liquid distribution trough, and liquid distribution trough upper surface does not have diverter function, the drop dropping onto liquid distribution trough upper surface trickles downwards along liquid distribution trough upper surface in an uneven manner, thus affect the distributed effect of liquid distribution trough.
Utility model content
Technical problem to be solved in the utility model is, for above-mentioned the deficiencies in the prior art, provides a kind of energy-efficient packed absorber.
The technical scheme that the energy-efficient packed absorber of the utility model adopts is as follows:
The packed absorber that the utility model is energy-efficient, comprise tower body, be provided with gas in tower body upper end and go out pipe, tower body lower end is provided with leakage fluid dram, tower body top is provided with the first temperature-measuring port, first pressure tap, thin liquid inlet pipe and liquid distribution trough, first temperature-measuring port, first pressure tap and thin liquid inlet pipe are all arranged on tower body lateral wall, liquid distribution trough is arranged on tower body inside and is connected with thin liquid inlet pipe, tower body lower outside wall is provided with the second temperature-measuring port, second pressure tap, gas inlet pipe and dope go out pipe, filler portion is provided with in tower body, described filler portion comprises packing layer, bed confinement plate and packing support plate, bed confinement plate and packing support plate are separately positioned on the upper and lower of packing layer, described liquid distribution trough comprises liquid distribution supervisor, store liquid case, branching block, several liquid distribution arms and second diffluence device, the upper end of liquid distribution supervisor is connected with thin liquid inlet pipe, the lower end of liquid distribution supervisor with store liquid case and be connected, the described liquid case that stores is that top in shape stores liquid case, several liquid distribution arms are arranged on and store on liquid lower box part sidewall, a shunting plug is provided with at the outlet end of each liquid distribution arm, shunting plug is evenly equipped with apopore, branching block sealing is arranged on Xu Ye case bottom centre, be provided with in branching block inside and disperse dress split channel, branching block top is provided with arc groove, vertical through holes is provided with in the middle part of branching block, described second diffluence device comprises the first bull stick, the second bull stick, the first bevel gear, the second bevel gear and shunting bucket, first bull stick is arranged in thin liquid inlet pipe, first bevel gear is arranged on the first bull stick front end, second bull stick is arranged in liquid distribution supervisor, second bull stick is anterior is exposed to branching block lower surface through the vertical through holes be positioned in the middle part of branching block, shunting bucket is arranged on the second bull stick front end, shunting bucket is evenly provided with several tap holes, second bevel gear is arranged on the rear end of the second bull stick, and the first bevel gear and the second bevel gear are connected with a joggle, be positioned at gas and go out pipe bottom and be provided with demister in tower body, described demister comprises gas branch pipe, demister urceolus, annular end cap, demister inner core, gas collection bucket, at least three layers of sieve bucket and at least three lamination pendular rings, demister inner core is fixed on demister outer barrel by annular end cap, the lower end going out gas branch pipe is connected with the upper end at demister inner core, the upper end going out gas branch pipe is connected with the air inlet that gas goes out pipe, and go out gas branch pipe and go out pipe with demister inner core and gas and communicate, gas collection bucket is arranged on demister inner core lower end, it is inner that sieve bucket is arranged on demister inner core, liquid trap ring is arranged on demister outer barrel, and liquid trap ring is positioned at sieve bucket below.
Pipe is gone out by arranging gas in tower body upper end, leakage fluid dram, first temperature-measuring port, first pressure tap, thin liquid inlet pipe, liquid distribution trough, demister, second temperature-measuring port, second pressure tap, gas inlet pipe and dope go out pipe, liquid enters into liquid distribution trough from the thin liquid inlet pipe being positioned at tower body top, sprinkling cloth liquid is carried out again through liquid distribution trough, the current spraying cloth liquid are fallen in the filler portion that is positioned in the middle part of tower body, trickled downwards by filler portion again, go out pipe finally by dope to flow out, gas enters into tower body from the gas inlet pipe being positioned at tower body bottom, form ascending air thereupon, through being positioned at the filler portion in the middle part of tower body, liquids and gases fully contact purification in filler portion, then air-flow continues to rise and the mist in ascending air and the liquid phase of carrying secretly to be separated through demister, air-flow after separation goes out pipe from gas and flows out.By filler portion being arranged to the version comprising packing layer, bed confinement plate and packing support plate, packing support plate is used for supporting packing layer, bed confinement plate is used for limiting the height of packing layer, and packing layer is fixed in tower body by bed confinement plate and the cooperation of packing support plate.
By liquid distribution trough being arranged to the version comprising liquid distribution supervisor, store liquid case, branching block, liquid distribution arm and second diffluence device, liquid enters in liquid distribution supervisor from thin liquid inlet pipe, again through liquid distribution supervisor flow into be positioned at liquid distribution supervisor lower end store liquid case, and from be positioned at the liquid distribution arm stored outside liquid lower box part carry out shunting outflow.By arranging arc groove on branching block top, be provided with in branching block inside and disperse dress split channel, the liquid stored in liquid case carries out dispersing shunting from the dress split channel of dispersing being positioned at branching block inside, liquid is prevented to be pooled in the middle part of distributor, by arranging second diffluence device, second diffluence device can carry out second diffluence to the liquid dropping into second diffluence device on a small quantity, makes liquid distribution even, thus improves the efficiency of gas-liquid exchange.By second diffluence device is arranged to comprise the first bull stick, second bull stick, first bevel gear, the version of the second bevel gear and shunting bucket, during the first bar rotation, drive the first bevel gear synchronous axial system being positioned at the first bull stick front end, thus drive the second bevel-gear rotating be meshed with the first bevel gear, second bevel gear drives the second bull stick synchronous axial system in rotation process, thus drive the shunting bucket being positioned at the second bull stick lower end to rotate, when liquid drops in shunting bucket, the shunting of rotation spray-type can be carried out to liquid by the rotation of shunting bucket, make shunting evenly.
By arranging demister, demister is used for the mist in ascending air and the liquid phase of carrying secretly to be separated.By demister is arranged to comprise gas branch pipe, demister urceolus, annular end cap, demister inner core, gas collection bucket, the version of sieve bucket and liquid trap ring, ascending air is collected by gas collection bucket, and upwards flow in demister inner core, by the sieve bucket that is positioned at demister inner core, mist and the liquid phase of carrying secretly are separated, the headwall that the drop formed after being separated tilts along sieve bucket glides to edge, flow into through demister inner core and be positioned at, in the demister urceolus of demister inner core outside, liquid trap ring again through being positioned at demister urceolus is collected, drop after collection trickles under forming current direction, fall on gas collection bucket outer wall, and guide by downward-sloping gas collection bucket outer wall and shunt, not only play equally distributed effect also can not drop onto on liquid distribution trough.
As preferred version of the present utility model, the quantity of described sieve bucket is five layers, and five layers of sieve bucket are disposed in demister inner core up and down, and the quantity of liquid trap ring is five layers, and five lamination pendular rings are disposed in demister urceolus up and down.
As preferred version of the present utility model, between neighbouring two layer screen bucket, be filled with wire or the plastic cement silk of intensive setting.
As preferred version of the present utility model, described demister inner core is rolled by wire netting and forms.
As preferred version of the present utility model, the headwall that described gas collection bucket is positioned at inside, demister inner core lower end is provided with air admission hole.
As preferred version of the present utility model, the headwall upper surface that described gas collection bucket is positioned at outside, demister inner core lower end is provided with diversion groove.
As preferred version of the present utility model, described liquid trap ring is concave shaped liquid trap ring, in the middle part of concave shaped liquid trap ring, be provided with annular fluid hole.
As preferred version of the present utility model, in the middle part of tower body, lateral wall is provided with at least one access hole, access hole is provided with upper cover.
As preferred version of the present utility model, be vertically disposed with the first liquid level meter interface and the second liquid level meter interface in tower body bottom, the first liquid level meter interface is connected with liquid level gauge with the second liquid level meter interface.
As preferred version of the present utility model, described liquid level counts gauge glass or magnetic fluid level gauge.
In sum, the advantage of the packed absorber that the utility model is energy-efficient is,
Liquid distribution is evenly distributed, and distributed effect is good, and the liquid water stream distributed can not to be pooled in the middle part of liquid distribution trough thus to improve the contact of liquids and gases in filler, thus improves gas-liquid and exchange effect.
Can be separated at the mist produced after filler and the liquid phase be entrained in air-flow ascending air, the mist compared with small particle diameter can also be separated, improve separative efficiency, thus improve the purity of giving vent to anger, and the drop formed in foam removal process can carry out collecting, shunting, not only play equally distributed effect, also can not drop onto on liquid distribution trough, thus extend the service life of liquid distribution trough.
Accompanying drawing explanation
Fig. 1 is the front view of the energy-efficient packed absorber of the utility model.
Fig. 2 is the structural representation of the liquid distribution trough of the energy-efficient packed absorber of the utility model.
Fig. 3 is the structural representation of the demister of the energy-efficient packed absorber of the utility model.
Detailed description of the invention
As shown in drawings, the packed absorber that the utility model is energy-efficient, comprise tower body 1, tower body 1 upper end is provided with gas and goes out pipe 2, tower body 1 lower end is provided with leakage fluid dram 3, tower body 1 top is provided with the first temperature-measuring port 4, first pressure tap 5, thin liquid inlet pipe 6 and liquid distribution trough, first temperature-measuring port 4, first pressure tap 5 and thin liquid inlet pipe 6 are all arranged on tower body 1 lateral wall, liquid distribution trough is arranged on tower body 1 inside and is connected with thin liquid inlet pipe 6, tower body 1 lower outside wall is provided with the second temperature-measuring port 7, second pressure tap 8, gas inlet pipe 9 and dope go out pipe 10, filler portion is provided with in tower body 1.
Pipe 2 is gone out by arranging gas in tower body 1 upper end, leakage fluid dram 3, first temperature-measuring port 4, first pressure tap 5, thin liquid inlet pipe 6, liquid distribution trough, demister, second temperature-measuring port 7, second pressure tap 8, gas inlet pipe 9 and dope go out pipe 10, liquid enters into liquid distribution trough from the thin liquid inlet pipe 6 being positioned at tower body 1 top, sprinkling cloth liquid is carried out again through liquid distribution trough, the current spraying cloth liquid are fallen in the filler portion that is positioned in the middle part of tower body 1, trickled downwards by filler portion again, go out pipe 10 finally by dope to flow out, gas enters into tower body 1 from the gas inlet pipe 9 being positioned at tower body 1 bottom, form ascending air thereupon, through being positioned at the filler portion in the middle part of tower body 1, liquids and gases fully contact purification in filler portion, then air-flow continues to rise and the mist in ascending air and the liquid phase of carrying secretly to be separated through demister, air-flow after separation goes out pipe 2 from gas and flows out.
Described filler portion comprises packing layer 11, bed confinement plate 12 and packing support plate 13, and bed confinement plate 12 and packing support plate 13 are separately positioned on the upper and lower of packing layer 11.By filler portion being arranged to the version comprising packing layer, bed confinement plate and packing support plate, packing support plate 13 is for supporting packing layer 11, bed confinement plate 12 is for limiting the height of packing layer 11, and bed confinement plate 12 and packing support plate 13 coordinate and be fixed in tower body 1 by packing layer 11.
Liquid distribution trough comprises liquid distribution supervisor 14, store liquid case 15, branching block 16, several liquid distribution arms 17 and second diffluence device, the upper end of liquid distribution supervisor 14 is connected with thin liquid inlet pipe 6, the lower end of liquid distribution supervisor 14 with store liquid case 15 and be connected, describedly store liquid case 15 for top in shape and store liquid case, several liquid distribution arms 17 are arranged on and store on liquid case 15 lower sides, a shunting plug is provided with at the outlet end of each liquid distribution arm 17, shunting plug is evenly equipped with apopore, branching block 16 sealing is arranged on Xu Yexiang 15 bottom centre, be provided with in branching block 16 inside and disperse dress split channel, branching block 16 top is provided with arc groove, vertical through holes is provided with in the middle part of branching block 16.
By liquid distribution trough being arranged to the version comprising liquid distribution supervisor, store liquid case, branching block, liquid distribution arm and second diffluence device, liquid enters in liquid distribution supervisor 14 from thin liquid inlet pipe 6, again through liquid distribution supervisor 14 flow into be positioned at liquid distribution supervisor lower end store liquid case 15, and from be positioned at the liquid distribution arm 17 storing liquid case 15 lower outside carry out shunting outflow.By arranging arc groove on branching block 16 top, be provided with in branching block 16 inside and disperse dress split channel, the liquid stored in liquid case 15 carries out dispersing shunting from the dress split channel of dispersing being positioned at branching block 16 inside, liquid is prevented to be pooled in the middle part of distributor, by arranging second diffluence device, second diffluence device can carry out second diffluence to the liquid dropping into second diffluence device on a small quantity, makes liquid distribution even, thus improves the efficiency of gas-liquid exchange.
Described second diffluence device comprises the first bull stick 18, second bull stick 19, first bevel gear 20, second bevel gear 21 and shunting bucket 22, first bull stick 18 is arranged in thin liquid inlet pipe 6, first bevel gear 20 is arranged on the first bull stick 18 front end, second bull stick 19 is arranged in liquid distribution supervisor 14, second bull stick 19 front portion is through the vertical through holes be positioned in the middle part of branching block 16 and be exposed to branching block 16 lower surface, shunting bucket 22 is arranged on the second bull stick 19 front end, shunting bucket 22 is evenly provided with several tap holes, second bevel gear 21 is arranged on the rear end of the second bull stick 19, first bevel gear 20 and the second bevel gear 21 are connected with a joggle.
By second diffluence device is arranged to comprise the first bull stick, second bull stick, first bevel gear, the version of the second bevel gear and shunting bucket, when first bull stick 18 rotates, drive the first bevel gear 20 synchronous axial system being positioned at the first bull stick 18 front end, thus drive the second bevel gear 21 be meshed with the first bevel gear 20 to rotate, second bevel gear 21 drives the second bull stick 19 synchronous axial system in rotation process, thus drive the shunting bucket 22 being positioned at the second bull stick 19 lower end to rotate, when liquid drops in shunting bucket 22, the shunting of rotation spray-type can be carried out to liquid by the rotation of shunting bucket 22, make shunting evenly.
Be positioned at gas and go out pipe bottom and be provided with demister in tower body 1, described demister comprises gas branch pipe 23, demister urceolus 24, annular end cap 25, demister inner core 26, gas collection bucket 27, at least three layers of sieve bucket 28 and at least three lamination pendular rings 29, described demister inner core 26 is rolled by wire netting and forms, it is inner that demister inner core 26 is fixed on demister urceolus 24 by annular end cap 25, the lower end going out gas branch pipe 23 is connected with the upper end at demister inner core 26, the upper end going out gas branch pipe 23 is connected with the air inlet that gas goes out pipe 2, and go out gas branch pipe 23 and go out pipe 2 with demister inner core 26 and gas and communicate, gas collection bucket 27 is arranged on demister inner core 26 lower end, the headwall being positioned at inside, demister inner core 26 lower end at gas collection bucket 27 is provided with air admission hole, the headwall upper surface being positioned at outside, demister inner core 26 lower end at gas collection bucket 27 is provided with diversion groove.It is inner that sieve bucket 28 is arranged on demister inner core 26, and it is inner that liquid trap ring 29 is arranged on demister urceolus 24, and liquid trap ring 29 is positioned at below sieve bucket 28, and described liquid trap ring 29 is concave shaped liquid trap ring, in the middle part of concave shaped liquid trap ring, be provided with annular fluid hole.
By arranging demister, demister is used for the mist in ascending air and the liquid phase of carrying secretly to be separated.By demister is arranged to comprise gas branch pipe, demister urceolus, annular end cap, demister inner core, gas collection bucket, the version of sieve bucket and liquid trap ring, ascending air is collected by gas collection bucket 27, and upwards flow in demister inner core 26, be separated by struggle against 28 pairs of mists and the liquid phase of carrying secretly of the sieve being positioned at demister inner core 26, the headwall that the drop formed after being separated tilts along sieve bucket 28 glides to edge, flow into through demister inner core 26 and be positioned at, in the demister urceolus 24 of demister inner core 26 outside, liquid trap ring 29 again through being positioned at demister urceolus 24 is collected, drop after collection trickles under forming current direction, fall on gas collection bucket 27 outer wall, and guide by downward-sloping gas collection bucket 27 outer wall and shunt, not only play equally distributed effect also can not drop onto on liquid distribution trough.
The quantity of described sieve bucket 28 is preferably five layers, and five layers of sieve bucket are disposed in demister inner core 26 up and down, and the quantity of liquid trap ring 29 is preferably five layers, and five lamination pendular rings are disposed in demister urceolus 24 up and down.
Wire or the plastic cement silk of intensive setting is preferably filled with between neighbouring two layer screen bucket 28.Wire or plastic cement silk can be separated tiny mist further, improve separating effect.
Lateral wall is provided with at least one access hole 30 in the middle part of tower body, access hole 30 is provided with upper cover 31.The first liquid level meter interface 32 is vertically disposed with and the second liquid level meter interface 33, first liquid level meter interface 32 is connected with liquid level gauge with the second liquid level meter interface 33 in tower body 1 bottom.Described liquid level counts gauge glass or magnetic fluid level gauge.
Below by reference to the accompanying drawings preferred embodiment of the present utility model is elaborated, but the utility model is not limited to above-mentioned embodiment, in the ken that art technical staff possesses, various change can also be made under the prerequisite not departing from the utility model aim.
Claims (10)
1. an energy-efficient packed absorber, comprise tower body (1), it is characterized in that: be provided with gas in tower body (1) upper end and go out pipe (2), tower body (1) lower end is provided with leakage fluid dram (3), tower body (1) top is provided with the first temperature-measuring port (4), first pressure tap (5), thin liquid inlet pipe (6) and liquid distribution trough, first temperature-measuring port (4), first pressure tap (5) and thin liquid inlet pipe (6) are all arranged on tower body (1) lateral wall, liquid distribution trough is arranged on tower body (1) inside and is connected with thin liquid inlet pipe (6), tower body (1) lower outside wall is provided with the second temperature-measuring port (7), second pressure tap (8), gas inlet pipe (9) and dope go out pipe (10), filler portion is provided with in tower body (1), described filler portion comprises packing layer (11), bed confinement plate (12) and packing support plate (13), bed confinement plate (12) and packing support plate (13) are separately positioned on the upper and lower of packing layer (11), described liquid distribution trough comprises liquid distribution supervisor (14), store liquid case (15), branching block (16), several liquid distribution arm (17) and second diffluence devices, the upper end of liquid distribution supervisor (14) is connected with thin liquid inlet pipe (6), the lower end of liquid distribution supervisor (14) with store liquid case (15) and be connected, describedly store liquid case (15) for top in shape and store liquid case, several liquid distribution arms (17) are arranged on and store on liquid case (15) lower sides, a shunting plug is provided with at the outlet end of each liquid distribution arm (17), shunting plug is evenly equipped with apopore, branching block (16) sealing is arranged on and stores liquid case (15) bottom centre, be provided with in branching block (16) inside and disperse dress split channel, branching block (16) top is provided with arc groove, branching block (16) middle part is provided with vertical through holes, described second diffluence device comprises the first bull stick (18), second bull stick (19), first bevel gear (20), second bevel gear (21) and shunting bucket (22), first bull stick (18) is arranged in thin liquid inlet pipe (6), first bevel gear (20) is arranged on the first bull stick (18) front end, second bull stick (19) is arranged in liquid distribution supervisor (14), the anterior vertical through holes through being positioned at branching block (16) middle part of second bull stick (19) is also exposed to branching block lower surface, shunting bucket (22) is arranged on the second bull stick (19) front end, shunting bucket (22) is evenly provided with several tap holes, second bevel gear (21) is arranged on the rear end of the second bull stick (19), first bevel gear (20) and the second bevel gear (21) are connected with a joggle, be positioned at gas and go out pipe bottom and be provided with demister in tower body (1), described demister comprises gas branch pipe (23), demister urceolus (24), annular end cap (25), demister inner core (26), gas collection bucket (27), at least three layers of sieve bucket (28) and at least three lamination pendular ring (29), it is inner that demister inner core (26) is fixed on demister urceolus (24) by annular end cap (25), the lower end going out gas branch pipe (23) is connected with the upper end at demister inner core (26), the upper end going out gas branch pipe (23) is connected with the air inlet that gas goes out to manage (2), and go out gas branch pipe (23) and go out to manage (2) with demister inner core (26) and gas and communicate, gas collection bucket (27) is arranged on demister inner core (26) lower end, it is inner that sieve bucket (28) is arranged on demister inner core (26), it is inner that liquid trap ring (29) is arranged on demister urceolus (24), and liquid trap ring (29) is positioned at sieve bucket (28) below.
2. energy-efficient packed absorber according to claim 1, it is characterized in that: the quantity of described sieve bucket (28) is five layers, five layers of sieve bucket are disposed in demister inner core (26) up and down, the quantity of liquid trap ring (29) is five layers, and five lamination pendular rings are disposed in demister urceolus (24) up and down.
3. energy-efficient packed absorber according to claim 2, is characterized in that: between neighbouring two layer screen bucket (28), be filled with intensive setting wire or plastic cement silk.
4. energy-efficient packed absorber according to claim 1, is characterized in that: described demister inner core (26) is rolled by wire netting and forms.
5. energy-efficient packed absorber according to claim 1, is characterized in that: the headwall that described gas collection bucket (27) is positioned at inside, demister inner core lower end is provided with air admission hole.
6. energy-efficient packed absorber according to claim 1, is characterized in that: the headwall upper surface that described gas collection bucket (27) is positioned at outside, demister inner core lower end is provided with diversion groove.
7. energy-efficient packed absorber according to claim 1, is characterized in that: described liquid trap ring (29) is concave shaped liquid trap ring, in the middle part of concave shaped liquid trap ring, be provided with annular fluid hole.
8. energy-efficient packed absorber according to claim 1, is characterized in that: on the lateral wall of tower body (1) middle part, be provided with at least one access hole (30), access hole (30) is provided with upper cover (31).
9. energy-efficient packed absorber according to claim 1, it is characterized in that: be vertically disposed with the first liquid level meter interface (32) and the second liquid level meter interface (33) in tower body (1) bottom, the first liquid level meter interface (32) is connected with liquid level gauge with the second liquid level meter interface (33).
10. energy-efficient packed absorber according to claim 9, is characterized in that: described liquid level counts gauge glass or magnetic fluid level gauge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520402143.5U CN204710094U (en) | 2015-06-11 | 2015-06-11 | Energy-efficient packed absorber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520402143.5U CN204710094U (en) | 2015-06-11 | 2015-06-11 | Energy-efficient packed absorber |
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| Publication Number | Publication Date |
|---|---|
| CN204710094U true CN204710094U (en) | 2015-10-21 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520402143.5U Expired - Fee Related CN204710094U (en) | 2015-06-11 | 2015-06-11 | Energy-efficient packed absorber |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107774207A (en) * | 2017-12-04 | 2018-03-09 | 马鞍山瑞琪机械设备制造有限公司 | A kind of packed tower with dredging function |
| CN109069942A (en) * | 2016-05-03 | 2018-12-21 | 道达尔公司 | Extraneous gas mixing tube for liquid-gas osculating element |
| CN110801678A (en) * | 2019-11-19 | 2020-02-18 | 杭州小橙工业设计有限公司 | Dandelion-like self-dropping type filtering device for purifying heavily-polluted waste gas |
-
2015
- 2015-06-11 CN CN201520402143.5U patent/CN204710094U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109069942A (en) * | 2016-05-03 | 2018-12-21 | 道达尔公司 | Extraneous gas mixing tube for liquid-gas osculating element |
| CN107774207A (en) * | 2017-12-04 | 2018-03-09 | 马鞍山瑞琪机械设备制造有限公司 | A kind of packed tower with dredging function |
| CN110801678A (en) * | 2019-11-19 | 2020-02-18 | 杭州小橙工业设计有限公司 | Dandelion-like self-dropping type filtering device for purifying heavily-polluted waste gas |
| CN110801678B (en) * | 2019-11-19 | 2021-07-16 | 温岭市亚超童鞋业有限公司 | Dandelion-like self-dropping type filtering device for purifying heavily-polluted waste gas |
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