CN209109186U - A kind of regenerating molecular sieve air cooling condensation water discharge unit - Google Patents
A kind of regenerating molecular sieve air cooling condensation water discharge unit Download PDFInfo
- Publication number
- CN209109186U CN209109186U CN201821839423.2U CN201821839423U CN209109186U CN 209109186 U CN209109186 U CN 209109186U CN 201821839423 U CN201821839423 U CN 201821839423U CN 209109186 U CN209109186 U CN 209109186U
- Authority
- CN
- China
- Prior art keywords
- tower body
- molecular sieve
- cylinder
- disk
- drain
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Drying Of Gases (AREA)
Abstract
The utility model discloses a kind of regenerating molecular sieve air cooling condensation water discharge units, including tower body, liquid absorption mechanism and gas absorbing mechanism are installed, the inside of tower body is also equipped with molecular sieve, the inlet pipe communicated with inner cavity and outlet pipe are further fixed on the two sidewalls of tower body at the top of the tower body；The liquid absorption mechanism is made of cylinder, motor, support plate and absorption disk, and cylinder is mounted on tower body, and support plate is fixed in the cylinder rod port of cylinder.This molecular sieve regeneration gas condensate drain, disk is absorbed to rise or decline under the driving of cylinder, motor drives motor shaft and rotating cylinder simultaneously, disk is absorbed since the negative pressure of suction hole drains the condensed water being located in tower body inner wall along drainage channel, rotating cylinder from flexible pipe, air inlet pipe absorbs the moisture and nitrogen that gasify in tower body, is then discharged out to drain, liquid level detector automatically controlled water pump, the workload of employee is reduced, and brings certain economic benefit.
Description
Technical field
The utility model relates to molecular sieve condensed water technical field, specially a kind of regenerating molecular sieve gas condensed water elimination dress
It sets.
Background technique
Molecular sieve has the Water Molecular Adsorption of part since irregular movement is adsorbed on condensation during regeneration gas
On the inner wall of tower, a large amount of hydrone just will form the water droplet of bulky grain during continuous aggregation, to regenerating molecular sieve
During aspiration, since bulky grain water droplet has certain gravity, negative pressure used is absorbed, it not necessarily can be by water droplet
It fully absorbs, the device of this respect and technique is not handled, cause what is absorbed to be not thorough.
Original design condensed water elimination is manual drain mode, finds there is discharge not in time by actual motion, causes cold
Condensate position is excessively high, causes liquid stifled, influences the discharge of regenerating molecular sieve gas, causes process conditions to fluctuate, to influence to produce, in addition stop
Pump not in time, can make emptying pump long-play, cause water level too low, destroy water seal, and a large amount of regeneration nitrogen can go here and there to discharge
Hole is outer, brings some potential safety problems, and there are also when especially making Summer Heavy Rainfall, a water pump can not produce needs.
Utility model content
The purpose of this utility model is to provide a kind of regenerating molecular sieve air cooling condensation water discharge units, including having to liquefaction
The water and nitrogen progress double-absorption of condensed water, gasification in the lumen on wall, while being drained into and being followed using self-draining control
Ring pond, solves the problems of the prior art at the advantages of bringing certain economic benefit.
To achieve the above object, the utility model provides the following technical solutions: a kind of regenerating molecular sieve gas condensed water elimination
Device, including tower body are equipped with liquid absorption mechanism and gas absorbing mechanism at the top of the tower body, and the inside of tower body is also installed
There is molecular sieve, the inlet pipe communicated with inner cavity and outlet pipe are further fixed on the two sidewalls of tower body；
The liquid absorption mechanism is made of cylinder, motor, support plate and absorption disk, and cylinder is mounted on tower body, branch
Fagging is fixed in the cylinder rod port of cylinder, and motor is disposed on the supporting plate by bolt, and the motor shaft port of motor passes through
Support plate is welded with anchorage bar, and motor is connected by anchorage bar with the port of rotating cylinder, the rotating cylinder and motor shaft on the outside of anchorage bar
Junction is cased with the positioning ring by ball flexible connection, and the absorption disk offers drainage around lateral circle surface and top circumferential surface and leads to
Road, is glued with heating sheet on the inside of drainage channel, rotating cylinder be connected to the center point for absorbing disk top circumferential surface and with internal drainage
Channel communicates；
The gas absorbing mechanism is by aspiration pump, flexible pipe, air inlet pipe and exhaust pipe group at aspiration pump is fixed on tower body
One end of top, air inlet pipe and flexible pipe with pumping pump inlet be connected, the other end of air inlet pipe is connected with tower body, flexible pipe it is another
One end pass through positioning ring communicated with rotating cylinder, one end of the exhaust pipe is connected with the outlet of aspiration pump, the other end of exhaust pipe with
Drain is connected, and the side wall of drain is equipped with liquid level detector, and the bottom of drain is also connected with the pipeline being connected with water pump.
Preferably, the tower body, which is located at below molecular sieve, is also equipped with the pipeline being connected with external high temperature heater.
Preferably, the quantity of the liquid level detector is two, is located at the top and bottom of the inner wall of drain, liquid
Bit detector is electrically connected with water pump by control line, and the water outlet of water pump is connected with circulatory pool.
Preferably, the diameter for absorbing disk is adapted with inner diameter of tower, is absorbed on the lateral circle surface and top circumferential surface of disk
Offer the suction hole communicated with drainage channel.
Compared with prior art, the beneficial effects of the utility model are as follows:
1. molecular sieve regeneration gas condensate drain changes and divides by the method for heating after high temperature heater (HTH) work
Saturated vapor pressure in the saturated vapor pressure and extraneous gas phase of son sieve phase water, so that mass transfer force is provided, it will be in molecular sieve
It is saturated water to tower body, partially due to the irregular movement of hydrone is adsorbed on inner wall and becomes water droplet, absorbs disk in gas
Rise under the driving of cylinder or decline, while motor drives motor shaft and rotating cylinder, absorbs disk since the negative pressure of suction hole is by position
Drain from flexible pipe in the condensed water in tower body inner wall along drainage channel, rotating cylinder, is then discharged out to drain.
2. molecular sieve regeneration gas condensate drain, the other end of air inlet pipe are connected with tower body, gasify in tower body
Moisture and nitrogen are absorbed, and drain is expelled to after aspiration pump extraction, and the side wall of drain is equipped with liquid level detector, according to
The position of the pre-set liquid level detector of process conditions, control system of setting out when water level reaches the liquid level detector of the upper limit is certainly
Dynamic starting water pump, when the liquid level detector that water level reaches lower limit is automatically stopped water pump, to achieve the purpose that automatic-discharging, into one
Auto-drainage is introduced circulating water pool by step optimization, and recycling and reusing not only solves the problems, such as discharge not in time in this way, also can
The workload of employee is reduced, and brings certain economic benefit.
Detailed description of the invention
Fig. 1 is the overall top view of the utility model；
Fig. 2 is the absorption disk decline state diagram of the utility model；
Fig. 3 is the absorption disk propradation figure of the utility model；
Fig. 4 is the gas absorbing mechanism perspective view of the utility model；
Fig. 5 is the gas absorbing mechanism internal structure chart of the utility model.
In figure: 1, tower body；11, molecular sieve；12, inlet pipe；13, outlet pipe；2, liquid absorption mechanism；21, cylinder；22, motor；
221, anchorage bar；23, support plate；24, disk is absorbed；241, drainage channel；242, heating sheet；3, gas absorbing mechanism；31, it takes out
Air pump；32, flexible pipe；33, air inlet pipe；34, exhaust pipe；4, rotating cylinder；5, positioning ring；6, suction hole；7, drain；71, liquid level
Detector；8, water pump.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
Please refer to Fig. 1-3, a kind of regenerating molecular sieve air cooling condensation water discharge unit, including tower body 1, the top installation of tower body 1
There are liquid absorption mechanism 2 and gas absorbing mechanism 3, the inside of tower body 1 is also equipped with molecular sieve 11, and molecular sieve 11 is separated
Afterwards, hydrone will stay in molecular sieve 11, and the inlet pipe 12 communicated with inner cavity and outlet pipe are further fixed on the two sidewalls of tower body 1
13, tower body 1, which is located at below molecular sieve 11, is also equipped with the pipeline being connected with external high temperature heater, leads to after high temperature heater (HTH) work
The method for crossing heating changes the saturated vapor pressure in the saturated vapor pressure and extraneous gas phase of 11 phase water of molecular sieve, to provide biography
Matter motive force, the saturation in molecular sieve 11 is water to tower body 1, partially due to the irregular movement of hydrone is adsorbed on inner wall
On become water droplet, liquid absorption mechanism 2 is by cylinder 21, motor 22, support plate 23 and absorbs disk 24 and forms, and cylinder 21 is mounted on
On tower body 1, support plate 23 is fixed in the cylinder rod port of cylinder 21, and motor 22 is placed in support plate 23 by bolt, gas
Cylinder 21 drives support plate 23 and motor 22 to rise or decline, and the motor shaft port of motor 22 passes through support plate 23 and is welded with fastening
Bar 221, motor 22 are connected by anchorage bar 221 with the port of rotating cylinder 4, and anchorage bar 221 connects the motor shaft of motor 22 and rotating cylinder 4
It is connected into an entirety, the frequency of rotation is identical, and the rotating cylinder 4 in 221 outside of anchorage bar and the junction of motor shaft are cased with and pass through ball
The positioning ring 5 of flexible connection, the two can be rotated around positioning ring 5, and ball reduces frictional force when rotation, while positioning ring
5 remain stationary it is motionless, avoid flexible pipe 32 occur winding problem, absorb disk 24 around lateral circle surface and top circumferential surface offers drainage
Channel 241, the inside of drainage channel 241 are glued with heating sheet 242, and heating sheet 242 carries out the liquid inside drainage channel 241
Heating, promotion, which is gasified, improves the ability of absorption, and rotating cylinder 4 is connected to the center point for absorbing the top of disk 24 circumferential surface and the drainage with inside
Channel 241 communicates, and the diameter for absorbing disk 24 is adapted with 1 internal diameter of tower body, absorbs on the lateral circle surface and top circumferential surface of disk 24
The suction hole 6 communicated with drainage channel 241 is offered, disk 24 is absorbed and connects with 1 inner wall of tower body, absorbs disk 24 in cylinder 21
Driving under rise or decline, while motor 22 drives motor shaft and rotating cylinder 4, absorbs disk 24 simultaneously because suction hole 6
Negative pressure drains the condensed water being located on 1 inner wall of tower body along drainage channel 241, rotating cylinder 4 from flexible pipe 32, is then discharged out.
Fig. 4-5 is please referred to, gas absorbing mechanism 3 is by aspiration pump 31, flexible pipe 32, air inlet pipe 33 and 34 groups of exhaust pipe
At aspiration pump 31 is fixed at the top of tower body 1, and one end of air inlet pipe 33 and flexible pipe 32 is connected with 31 import of aspiration pump, aspiration pump
31 allow air inlet pipe 33 and the interior generation negative pressure of flexible pipe 32, the other end of air inlet pipe 33 to be connected with tower body 1, the water to gasify in tower body 1
Divide and nitrogen is absorbed, the other end of flexible pipe 32 passes through positioning ring 5 and communicates with rotating cylinder 4, since positioning ring 5 can and then rise
Or decline, flexible pipe 32 also can be and then changed, one end of exhaust pipe 34 is connected with the outlet of aspiration pump 31, exhaust pipe 34
The other end be connected with drain 7, aspiration pump 31 is expelled to drain 7 after extracting out, and the side wall of drain 7 is equipped with level sensing
Device 71, the quantity of liquid level detector 71 are two, are located at the top and bottom of the inner wall of drain 7, liquid level detector 71
Be electrically connected with water pump 8 by control line, the water outlet of water pump 8 is connected with circulatory pool, the bottom of drain 7 be also connected with and
The connected pipeline of water pump 8, according to the position of the pre-set liquid level detector 71 of process conditions, when water level reaches the liquid level of the upper limit
Control system of setting out when detector 71 starts water pump 8 automatically, when the liquid level detector 71 that water level reaches lower limit is automatically stopped water pump
7, to achieve the purpose that automatic-discharging, advanced optimize, Auto-drainage is introduced into circulating water pool, recycling and reusing, so not
But it solves the problems, such as discharge not in time, also can be reduced the workload of employee, and bring certain economic benefit.
In summary: this molecular sieve regeneration gas condensate drain, the method after high temperature heater (HTH) work by heating,
Change the saturated vapor pressure in the saturated vapor pressure and extraneous gas phase of 11 phase water of molecular sieve, to provide mass transfer force, will divide
The sub saturation sieved in 11 is water to inhale to tower body 1 partially due to the irregular movement of hydrone is adsorbed on inner wall and becomes water droplet
Receive disk 24 to rise or decline under the driving of cylinder 21, while the drive motor shaft and rotating cylinder 4 of motor 22, absorption disk 24 by
The condensed water being located on 1 inner wall of tower body is arranged from flexible pipe 32 along drainage channel 241, rotating cylinder 4 in the negative pressure of suction hole 6
It walks, is then discharged out, the other end of air inlet pipe 33 is connected with tower body 1, and the moisture and nitrogen to gasify in tower body 1 is absorbed, and is evacuated
Drain 7 is expelled to after 31 extraction of pump, the side wall of drain 7 is equipped with liquid level detector 71, presets according to process conditions
The position of good liquid level detector 71, control system of setting out when water level reaches the liquid level detector 71 of the upper limit start water pump 8 automatically,
When the liquid level detector 71 that water level reaches lower limit is automatically stopped water pump 7, to achieve the purpose that automatic-discharging, advanced optimize,
Auto-drainage is introduced into circulating water pool, recycling and reusing not only solves the problems, such as discharge not in time in this way, also can be reduced employee
Workload, and bring certain economic benefit.
It should be noted that, in this document, relational terms such as first and second and the like are used merely to a reality
Body or operation are distinguished with another entity or operation, are deposited without necessarily requiring or implying between these entities or operation
In any actual relationship or order or sequence.Moreover, the terms "include", "comprise" or its any other variant are intended to
Non-exclusive inclusion, so that the process, method, article or equipment including a series of elements is not only wanted including those
Element, but also including other elements that are not explicitly listed, or further include for this process, method, article or equipment
Intrinsic element.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is understood that these embodiments can be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaired
Change, replacement and variant, the scope of the utility model is defined by the appended claims and the equivalents thereof.
Claims (4)
- The condensation water discharge unit 1. a kind of regenerating molecular sieve is gas-cooled, including tower body (1), it is characterised in that: the top of the tower body (1) Liquid absorption mechanism (2) and gas absorbing mechanism (3) are installed, the inside of tower body (1) is also equipped with molecular sieve (11), tower body (1) inlet pipe (12) communicated with inner cavity and outlet pipe (13) are further fixed on two sidewalls；The liquid absorption mechanism (2) is made of cylinder (21), motor (22), support plate (23) and absorption disk (24), cylinder (21) it is mounted on tower body (1), support plate (23) is fixed in the cylinder rod port of cylinder (21), and motor (22) is pacified by bolt It sets on support plate (23), the motor shaft port of motor (22) passes through support plate (23) and is welded with anchorage bar (221), motor (22) It is connected by anchorage bar (221) with the port of rotating cylinder (4), the junction set of rotating cylinder (4) and motor shaft on the outside of anchorage bar (221) There is the positioning ring (5) by ball flexible connection, the absorption disk (24) offers drainage around lateral circle surface and top circumferential surface and leads to Road (241) is glued with heating sheet (242) on the inside of drainage channel (241), and rotating cylinder (4), which is connected to, absorbs disk (24) top circumferential surface The center point and communicated with internal drainage channel (241)；The gas absorbing mechanism (3) is made of aspiration pump (31), flexible pipe (32), air inlet pipe (33) and exhaust pipe (34), Aspiration pump (31) is fixed at the top of tower body (1), and one end of air inlet pipe (33) and flexible pipe (32) is connected with aspiration pump (31) import, The other end of air inlet pipe (33) is connected with tower body (1), and the other end of flexible pipe (32) passes through positioning ring (5) and communicates with rotating cylinder (4), One end of the exhaust pipe (34) is connected with the outlet of aspiration pump (31), and the other end of exhaust pipe (34) is connected with drain (7), The side wall of drain (7) is equipped with liquid level detector (71), and the bottom of drain (7) is also connected with the pipe being connected with water pump (8) Road.
- The condensation water discharge unit 2. a kind of regenerating molecular sieve according to claim 1 is gas-cooled, it is characterised in that: the tower body (1) it is located at below molecular sieve (11) and is also equipped with the pipeline being connected with external high temperature heater.
- The condensation water discharge unit 3. a kind of regenerating molecular sieve according to claim 1 is gas-cooled, it is characterised in that: the liquid level inspection The quantity for surveying device (71) is two, is located at the top and bottom of the inner wall of drain (7), and liquid level detector (71) is and water It pumps (8) to be electrically connected by control line, the water outlet of water pump (8) is connected with circulatory pool.
- The condensation water discharge unit 4. a kind of regenerating molecular sieve according to claim 1 is gas-cooled, it is characterised in that: the absorption circle The diameter of disk (24) is adapted with tower body (1) internal diameter, is absorbed and is offered and drain on the lateral circle surface and top circumferential surface of disk (24) The suction hole (6) that channel (241) communicates.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821839423.2U CN209109186U (en) | 2018-11-07 | 2018-11-07 | A kind of regenerating molecular sieve air cooling condensation water discharge unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821839423.2U CN209109186U (en) | 2018-11-07 | 2018-11-07 | A kind of regenerating molecular sieve air cooling condensation water discharge unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209109186U true CN209109186U (en) | 2019-07-16 |
Family
ID=67204332
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821839423.2U Expired - Fee Related CN209109186U (en) | 2018-11-07 | 2018-11-07 | A kind of regenerating molecular sieve air cooling condensation water discharge unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209109186U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115155249A (en) * | 2022-09-05 | 2022-10-11 | 济南德洋低温科技有限公司 | Method and device for recovering special gas adsorbed by molecular sieve |
-
2018
- 2018-11-07 CN CN201821839423.2U patent/CN209109186U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115155249A (en) * | 2022-09-05 | 2022-10-11 | 济南德洋低温科技有限公司 | Method and device for recovering special gas adsorbed by molecular sieve |
| CN115155249B (en) * | 2022-09-05 | 2022-12-02 | 济南德洋低温科技有限公司 | Method and device for recovering special gas adsorbed by molecular sieve |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206435006U (en) | A kind of waste gas purification environmental protection equipment | |
| CN113731128B (en) | High-efficiency natural gas dehydration treatment device and method | |
| CN209109186U (en) | A kind of regenerating molecular sieve air cooling condensation water discharge unit | |
| CN106870400A (en) | A kind of damping type swings water suction proof submersible sand discharging pump | |
| CN111632325B (en) | Fire hose winding device | |
| CN115057603A (en) | Cold evaporation humidification sludge drying device of adjustable wind speed | |
| CN112717640A (en) | Intelligent and efficient methyl chloride tail gas recovery device and use method thereof | |
| CN205870898U (en) | Perforating device with dust removal function | |
| CN209204702U (en) | A kind of glue experiment separating-purifying device | |
| CN209278144U (en) | A kind of adjustable-blade propeller pump | |
| CN208857222U (en) | A kind of device in Gas gas-liquid separation device | |
| CN207211307U (en) | A kind of municipal administration drainage arrangement | |
| CN202224009U (en) | Floating ball dust catcher with condensation water backflow | |
| CN208943499U (en) | A kind of organic exhaust gas active-carbon fibers adsorption processing unit | |
| CN205586652U (en) | Rotation type candle filter | |
| CN208943790U (en) | A kind of sludge drying distilled water removes ammonia nitrogen absorption tower | |
| CN209127472U (en) | A kind of sludge drying uniform dry mud conveying discharging device of drying | |
| CN203582824U (en) | Methane dehydration device | |
| CN207600124U (en) | Continuous disc drying machine | |
| CN207342910U (en) | A kind of cyclone gas-water separation device | |
| CN109025912A (en) | Coal bed gas water drainage gas production device | |
| CN206861505U (en) | A kind of pneumatic condensed-water recovering device | |
| CN216048743U (en) | Vacuum tower water trap | |
| CN217351056U (en) | Centrifugal kitchen garbage oil-water separator | |
| CN110683734A (en) | Efficient and energy-saving deep dehydration system based on dual-motor variable-frequency transmission water circulation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190716 Termination date: 20211107 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |