CN208512201U - A kind of new zeolite runner enrichment facility - Google Patents
A kind of new zeolite runner enrichment facility Download PDFInfo
- Publication number
- CN208512201U CN208512201U CN201821142570.4U CN201821142570U CN208512201U CN 208512201 U CN208512201 U CN 208512201U CN 201821142570 U CN201821142570 U CN 201821142570U CN 208512201 U CN208512201 U CN 208512201U
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- zeolite
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- side wall
- discharging pipe
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Abstract
The utility model discloses a kind of new zeolite runner enrichment facilities, including support frame, the center position of support frame as described above is provided with zeolite wheel, driving pulley is provided in front of the zeolite wheel, and zeolite wheel is rotatablely connected by belt and driving pulley, the right end of the driving pulley is provided with driving motor, left shell is provided on the left side of the zeolite wheel, and right shell body is provided on the right side of zeolite wheel, two cooling blowers are separately installed on the zeolite enrichment facility at left and right sides of runner, the two sides of zeolite can be cooled down simultaneously, improve cooling efficiency, and the hot wind of second cooling blower blowout enters the second cooling, air discharging pipe, second cooling, air discharging pipe is connect with concentration tube and heat exchanger tube respectively, can according to need discharge into concentration tube help be catalyzed burning, heat can also be exchanged by heat exchanger tube becomes room temperature Air-flow heel row dilutes the exhaust gas in flue gas leading into flue gas leading, improves zeolite to the adsorption rate of organic solvent.
Description
Technical field
The utility model belongs to gas exhaust treatment technical field, and in particular to a kind of new zeolite runner enrichment facility.
Background technique
Zeolite runner enrichment facility is one kind using ceramic fibre as substrate, and wheel surface is coated with hydrophobic zeolite and adsorbs
Agent, the cellular disc being made into can effectively adsorb the organic solvent in exhaust gas, can reach to the purification efficiency of exhaust gas
98% or more, but current zeolite runner enrichment facility still has a little shortcoming.
Current zeolite runner enrichment facility is equipped with cooling blower in the side of zeolite, since zeolite has two sides, meeting
Cause the cooling rate of the another side of zeolite slow, and effect is relatively low, if without completely cooling in time, after largely effecting on
Continuous adsorption effect；Although zeolite has hydrophobicity, it can all contain moisture in general exhaust gas, relatively even humidity can reach
To 80%, and when the exhaust gas of low concentration passes through zeolite, moisture can occupy adsorption space and influence the adsorption effect of organic solvent,
The problems such as equal, need us and solve.
Utility model content
The purpose of this utility model is to provide a kind of new zeolite runner enrichment facilities, to solve in above-mentioned background technique
The current zeolite runner enrichment facility proposed is equipped with cooling blower in the side of zeolite, since zeolite has two sides, can lead
Cause the cooling rate of the another side of zeolite slow, and effect is relatively low, if can largely effect on subsequent without completely cooling in time
Adsorption effect；Although zeolite has hydrophobicity, it can all contain moisture in general exhaust gas, relatively even humidity can reach
80%, and when the exhaust gas of low concentration passes through zeolite, moisture can occupy adsorption space and influence the adsorption effect of organic solvent
Problem.
To achieve the above object, the utility model provides the following technical solutions: a kind of new zeolite runner enrichment facility, packet
Support frame is included, the center position of support frame as described above is provided with zeolite wheel, is provided with driving pulley in front of the zeolite wheel, and
Zeolite wheel is rotatablely connected by belt and driving pulley, and the right end of the driving pulley is provided with driving motor, the zeolite wheel
Left side on be provided with left shell, and right shell body is provided on the right side of zeolite wheel, the left shell and right shell body it is interior
Portion is mounted on subregion frame, and concentration tube is provided with above left housing body sidewall, and it is cold to be provided with first in front of the concentration tube
But it manages, the first cooling blower is installed, it is cooling that the rear of the concentration tube is provided with second on the side wall of first cooling tube
Air-exhausting duct, and flue gas leading is provided with below concentration tube, the sidewall upper of the flue gas leading is equipped with cartridge filter by clip, institute
The inside for stating cartridge filter is equipped with metal filter screen, and the right end of the metal filter screen is equipped with PP cotton filtering layer, the right shell body
Side wall on heating tube is provided at concentration tube opposite position, heating component, institute are installed on the side wall of the heating tube
The right end for stating heating component is equipped with blower, on the side wall of the right shell body with is provided at the first cooling tube opposite position
One cooling, air discharging pipe, the first cooling, air discharging pipe is connect by the first solenoid valve with heating tube, on the side wall of the right shell body
It is provided with the second cooling tube at the second cooling, air discharging pipe opposite position, is equipped with second on the side wall of second cooling tube
Cooling blower, on the side wall of the right shell body be provided with exhaust pipe at flue gas leading opposite position, support frame as described above
Upper surface is equipped with control box, and the front surface of the control box is equipped with display screen, control is equipped with below the display screen
Switch, the control box are internally provided with controller, are provided with timer in front of the controller, the driving motor,
First cooling blower, heating component, the first solenoid valve, the second cooling blower, display screen, controller and timer are opened with control
It closes and is electrically connected, the control switch is electrically connected by power outlet and extraneous power supply.
Preferably, the right end of the cartridge filter is provided with water-absorbing cylinder, and the water-absorbing cylinder connects by the way that clip and flue gas leading are fixed
It connects, the water-absorbing cylinder is internally provided with falope ring.
Preferably, heat exchanger tube is provided with below the second cooling, air discharging pipe, and the second cooling, air discharging pipe passes through three
Three-way magnetic valve is connect with heat exchanger tube and concentration tube respectively, and the 3-position-3-way solenoid valve and controller are electrically connected.
Preferably, stepper motor is installed, and exhaust pipe is internally provided with baffle on the side wall of the exhaust pipe, it is described
Baffle is mounted in the shaft of stepper motor, and baffle is circular configuration, the diameter of the baffle and the internal diameter diameter of exhaust pipe
Dimensional values are equal, and the stepper motor and controller are electrically connected.
Preferably, intensive fin is installed on the side wall of the heat exchanger tube, the heat exchanger tube by second solenoid valve with
Flue gas leading connection, the second solenoid valve and controller are electrically connected.
Compared with prior art, the utility model has the beneficial effects that on the zeolite enrichment facility runner the left and right sides
Two cooling blowers are separately installed with, the two sides of zeolite can be cooled down simultaneously, improve cooling efficiency, and second cold
But the hot wind of blower blowout enters the second cooling, air discharging pipe, and the second cooling, air discharging pipe is connect with concentration tube and heat exchanger tube respectively,
Can according to need discharge into concentration tube help be catalyzed burning, can also by heat exchanger tube exchange heat become unheated air heel row into
Flue gas leading dilutes the exhaust gas in flue gas leading, improves zeolite to the adsorption rate of organic solvent；And pacify in the water-absorbing cylinder in flue gas leading
Equipped with falope ring, falope ring can adsorb the moisture in exhaust gas, avoid moisture from occupying zeolite adsorption space, influence adsorption effect,
And falope ring is waveform, and the area that falope ring is close to inner wall is smaller, and exhaust gas can be made to pass through from the tow sides of falope ring,
Water-taking efficiency is substantially increased, and no barrier action is discharged into exhaust gas；Baffle is also equipped in exhaust pipe, baffle is by step
Into motor control, after exhaust gas enters in zeolite and adsorbs, since zeolite adsorption effect is influenced by revolving speed, so cannot
100% absorption, and baffle can increase the resistance to exhaust gas, extend exhaust gas in zeolite interior residence time, increase in exhaust gas
The contact probability of organic solvent and adsorption hole greatly improves the efficiency of absorption.
Detailed description of the invention
Fig. 1 is the utility model main view；
Fig. 2 is the left shell side structure schematic view of the utility model；
Fig. 3 is the left shell side cross-sectional, view of the utility model；
Fig. 4 is the partial left side view of the utility model；
Fig. 5 is the cartridge structure schematic diagram of the utility model；
Fig. 6 is the water-absorbing cylinder side cross-sectional, view of the utility model；
Fig. 7 is the exhaust pipe local overlooking structural schematic diagram of the utility model.
In figure: 1- support frame, 2- zeolite wheel, 3- driving pulley, 4- driving motor, 5- left shell, 6- right shell body, 7- exhaust gas
Pipe, 8- cartridge filter, 9- water-absorbing cylinder, 10- exhaust pipe, 11- stepper motor, 12- concentration tube, 13- blower, 14- heating tube, 15- add
Hot component, the first cooling tube of 16-, the first cooling blower of 17-, the first cooling, air discharging of 18- pipe, the second cooling tube of 19-, 20- second
Cooling blower, the second cooling, air discharging of 21- pipe, 22- heat exchanger tube, 23- fin, 24- second solenoid valve, 25- subregion frame, 26- metal
Filter screen, 27-PP cotton filtering layer, 28- falope ring, 29- baffle, 30- control box, 31- display screen, 32- control switch, 33- control
Device, 34- timer, 35- 3-position-3-way solenoid valve, the first solenoid valve of 36-.
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.
Fig. 1-7 is please referred to, the utility model provides a kind of technical solution: a kind of new zeolite runner enrichment facility, including
Support frame 1, the center position of support frame 1 are provided with zeolite wheel 2, and the front of zeolite wheel 2 is provided with driving pulley 3, and zeolite
Wheel 2 is rotatablely connected by belt and driving pulley 3, and the right end of driving pulley 3 is provided with driving motor 4, the left side of zeolite wheel 2
On be provided with left shell 5, and right shell body 6 is provided on the right side of zeolite wheel 2, the inside of left shell 5 and right shell body 6 is respectively mounted
There is subregion frame 25, and be provided with concentration tube 12 above 5 side wall of left shell, the front of concentration tube 12 is provided with the first cooling tube
16, the first cooling blower 17 is installed on the side wall of the first cooling tube 16, the rear of concentration tube 12 is provided with the second cooling, air discharging
Pipe 21, and the lower section of concentration tube 12 is provided with flue gas leading 7, the sidewall upper of flue gas leading 7 is equipped with cartridge filter 8, mistake by clip
The inside of filter cylinder 8 is equipped with metal filter screen 26, and the right end of metal filter screen 26 is equipped with PP cotton filtering layer 27, the side of right shell body 6
On wall be provided with heating tube 14 at 12 opposite position of concentration tube, heating component 15 is installed on the side wall of heating tube 14, is added
The right end of hot component 15 is equipped with blower 13, on the side wall of right shell body 6 with is provided at 16 opposite position of the first cooling tube
One cooling, air discharging pipe 18, the first cooling, air discharging pipe 18 is connect by the first solenoid valve 36 with heating tube 14, on the side wall of right shell body 6
With the second cooling tube 19 is provided at 21 opposite position of the second cooling, air discharging pipe, is equipped on the side wall of the second cooling tube 19
Two cooling blowers 20, on the side wall of right shell body 6 with exhaust pipe 10, the upper table of support frame 1 are provided at 7 opposite position of flue gas leading
Face is equipped with control box 30, and the front surface of control box 30 is equipped with display screen 31, and the lower section of display screen 31 is equipped with control switch
32, control box 30 is internally provided with controller 33, and the front of controller 33 is provided with timer 34, and driving motor 4, first is cold
But blower 17, heating component 15, the first solenoid valve 36, the second cooling blower 20, display screen 31, controller 33 and timer 34 are equal
It is electrically connected with control switch 32, control switch 32 is electrically connected by power outlet and extraneous power supply.
In the present embodiment, it is preferred that the right end of cartridge filter 8 is provided with water-absorbing cylinder 9, and water-absorbing cylinder 9 passes through clip and flue gas leading 7
It is fixedly connected, it is a kind of high activity adsorbent material that water-absorbing cylinder 28, which is internally provided with falope ring 28, and silica gel refers to silicic acid gel, tool
There is superpower water sorption, falope ring 28 can adsorb the moisture in exhaust gas, the adsorption hole on moisture blocking zeolite wheel 2 is avoided,
The adsorption space for occupying Zeolites Zeolites wheel 2 influences adsorption effect, and falope ring 28 is waveform, falope ring 28 and water-absorbing cylinder 9
The area that inner wall is close to is smaller, and exhaust gas can be made to pass through from the tow sides of falope ring 28, substantially increase water-taking efficiency, and right
Exhaust gas passes through no barrier action.
In the present embodiment, it is preferred that the lower section of the second cooling, air discharging pipe 21 is provided with heat exchanger tube 22, and the second cooling, air discharging
Pipe 21 is connect with heat exchanger tube 22 and concentration tube 12 respectively by 3-position-3-way solenoid valve 35,3-position-3-way solenoid valve 35 and controller
33 are electrically connected, and there are two cooling device, the second cooling blower 20 in the second cooling tube 19 can be from zeolite for device setting
The another side of wheel 2 enters and cools down, and the hot wind of exchange heat is discharged into from the second cooling, air discharging pipe 21, while can pass through three
35 control piper of position-3-way solenoid valve, hot wind is drained into concentration tube 12, and help is catalyzed burning, can also discharge into heat exchanger tube 22
In, the exchange again of heat is carried out, the air-flow for being converted into room temperature utilizes.
In the present embodiment, it is preferred that stepper motor 11 is installed, and the inside of exhaust pipe 10 is set on the side wall of exhaust pipe 10
It is equipped with baffle 29, baffle 29 is mounted in the shaft of stepper motor 11, and baffle 29 is circular configuration, the diameter of baffle 29 and row
The internal diameter diameter dimension numerical value of tracheae 10 is equal, and stepper motor 11 and controller 33 are electrically connected, and enters zeolite wheel 2 in exhaust gas
Afterwards, since the adsorption effect of zeolite is also influenced by revolving speed, thus cannot 100% absorption, can control 11 turns of stepper motor
Dynamic baffle 29, and the edge of baffle 29 is fitted closely with 10 inner wall of exhaust pipe, the resistance to exhaust gas can be increased, prolonged
Long exhaust gas increases the contact probability of organic solvent and adsorption hole in exhaust gas, substantially increases suction in zeolite interior residence time
Baffle 29 is rotated 90 degree over time by Timer Controlling, it is empty to increase discharge by attached efficiency, stepper motor 11
Between, so that clean air is discharged.
In the present embodiment, it is preferred that intensive fin 23 is installed, heat exchanger tube 22 passes through second on the side wall of heat exchanger tube 22
Solenoid valve 24 is connect with flue gas leading 7, and second solenoid valve 24 and controller 33 are electrically connected, and fin 23 is to need to carry out hot transmitting
Heat-exchanger rig surface the stronger sheet metal of increase thermal conductivity；Heat exchanger tube 22 passes through fin 23 for internal thermal current and the external world
Air themperature in exchange after, the unheated air of generation can discharge into flue gas leading 7, and dilution is next time by useless in flue gas leading 7
Gas improves zeolite to the adsorption rate of organic solvent.
Working principle: when the utility model is used, user's cognition is closed to the first solenoid valve 36, and second solenoid valve 24 is closed
It closes, 3-position-3-way solenoid valve 35 is closed, and is powered on first, and start driving motor 4, drives driving pulley 3 to rotate, main belt
Wheel 3 drives zeolite wheel 2 to rotate by belt, while exhaust gas is passed through when exhaust gas passes through cartridge filter 8 first by flue gas leading 7
Metal filter screen 26 intercepts biggish impurity, and filters lesser impurity by PP cotton filtering layer 27, then and by water-absorbing cylinder 9,
Internal falope ring 28 can adsorb the moisture in exhaust gas, avoid the adsorption hole on moisture blocking zeolite wheel 2, occupy Zeolites Zeolites
The adsorption space of wheel 2 influences adsorption effect, and falope ring 28 is waveform, the face that falope ring 28 is close to the inner wall of water-absorbing cylinder 9
Product is smaller, and exhaust gas can be made to pass through from the tow sides of falope ring 28, substantially increases water-taking efficiency, and to exhaust gas by not
There is barrier action, then exhaust gas is by left shell 5, and the inside by entering zeolite wheel 2 by the region that subregion frame 25 separates,
It is adsorbed, and is discharged from the exhaust pipe 10 on right shell body 6, while can control 11 flap shutter 29 of stepper motor, and make
The edge of baffle 29 can be fitted closely with 10 inner wall of exhaust pipe, can increase the resistance to exhaust gas, extend exhaust gas in zeolite
Portion's residence time increases the contact probability of organic solvent and adsorption hole in exhaust gas, substantially increases the efficiency of absorption, stepping electricity
Baffle 29 is rotated 90 degree over time by Timer Controlling by machine 11, increases discharge space, so that clean air is arranged
Out, it after adsorbing a period of time, can star heating component 15, improve the temperature inside heating tube 14, and start blower 13, to
Hot wind is formed when the air-flow being blown into heating tube 14 is by heating up component 15, and by being divided inside right shell body 6 by subregion frame 25
Every region, and pass through zeolite wheel 2, the adsorption hole on zeolite will be made to become larger, and organic solvent is detached from from adsorption hole,
And be blown into concentration tube 12, it is discharged in burner, then starts the first cooling blower 17 and the second cooling blower 20, make
Stream bring about the desired sensation respectively from the first cooling tube 16 and the second cooling tube 19 by the inside of zeolite wheel 2, zeolite is cooled down, Ke Yitong
When the two sides of zeolite is cooled down, improve cooling efficiency, open simultaneously the first solenoid valve 36, so that the first cooling blower 17
The air-flow of generation enters in heating tube 14 after the first cooling, air discharging pipe 8, and is drained into burning dress by concentration tube 12
In setting, while the hot wind for exchanging heat is discharged into from the second cooling, air discharging pipe 21, and user can open 3-position-3-way solenoid valve 35, together
When by 35 control piper of 3-position-3-way solenoid valve, hot wind is drained into concentration tube 12, help is catalyzed burning, can also discharge into
In heat exchanger tube 22, the exchange again of heat is carried out, the air-flow for being converted into room temperature utilizes, and heat exchanger tube 22 passes through fin 23 for inside
After being exchanged in thermal current and extraneous air themperature, the unheated air of generation, and second solenoid valve 24 is opened, discharged into exhaust gas
Pipe 7, dilution by the exhaust gas in flue gas leading 7, improve adsorption rate of the zeolite to organic solvent, entire workflow knot next time
Beam.
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 (5)
1. a kind of new zeolite runner enrichment facility, including support frame (1), it is characterised in that: the centre bit of support frame as described above (1)
The place of setting is provided with zeolite wheel (2), is provided with driving pulley (3) in front of the zeolite wheel (2), and zeolite wheel (2) passes through belt
It is rotatablely connected with driving pulley (3), the right end of the driving pulley (3) is provided with driving motor (4), the zeolite wheel (2)
Be provided on left side left shell (5), and be provided with right shell body (6) on the right side of zeolite wheel (2), the left shell (5) and
The inside of right shell body (6) is mounted on subregion frame (25), and is provided with concentration tube (12) above left shell (5) side wall, described
It is provided in front of concentration tube (12) the first cooling tube (16), it is cooling that first is equipped on the side wall of first cooling tube (16)
Blower (17), the rear of the concentration tube (12) are provided with the second cooling, air discharging pipe (21), and the lower section setting of concentration tube (12)
Have flue gas leading (7), the sidewall upper of the flue gas leading (7) is equipped with cartridge filter (8) by clip, the cartridge filter (8) it is interior
Portion is equipped with metal filter screen (26), and the right end of the metal filter screen (26) is equipped with PP cotton filtering layer (27), the right shell body
(6) it is provided with heating tube (14) on side wall at concentration tube (12) opposite position, pacifies on the side wall of the heating tube (14)
Equipped with heating component (15), the right end of the heating component (15) is equipped with blower (13), on the side wall of the right shell body (6) with
The first cooling, air discharging pipe (18) is provided at first cooling tube (16) opposite position, the first cooling, air discharging pipe (18) passes through
First solenoid valve (36) is connect with heating tube (14), opposite with the second cooling, air discharging pipe (21) on the side wall of the right shell body (6)
It answers and is provided at position the second cooling tube (19), the second cooling blower is installed on the side wall of second cooling tube (19)
(20), on the side wall of the right shell body (6) be provided with exhaust pipe (10), support frame as described above at flue gas leading (7) opposite position
(1) upper surface is equipped with control box (30), and the front surface of control box (30) is equipped with display screen (31), the display screen
(31) it is equipped with below control switch (32), control box (30) is internally provided with controller (33), the controller
(33) it is provided in front of timer (34), the driving motor (4), the first cooling blower (17), heating component (15), first
Solenoid valve (36), the second cooling blower (20), display screen (31), controller (33) and timer (34) with control switch (32)
It is electrically connected, the control switch (32) is electrically connected by power outlet and extraneous power supply.
2. a kind of new zeolite runner enrichment facility according to claim 1, it is characterised in that: the cartridge filter (8)
Right end is provided with water-absorbing cylinder (9), and the water-absorbing cylinder (9) is fixedly connected by clip with flue gas leading (7), the water-absorbing cylinder (9)
It is internally provided with falope ring (28).
3. a kind of new zeolite runner enrichment facility according to claim 1, it is characterised in that: second cooling, air discharging
Pipe (21) below be provided with heat exchanger tube (22), and the second cooling, air discharging pipe (21) by 3-position-3-way solenoid valve (35) respectively with
Heat exchanger tube (22) and concentration tube (12) connection, the 3-position-3-way solenoid valve (35) and controller (33) are electrically connected.
4. a kind of new zeolite runner enrichment facility according to claim 1, it is characterised in that: the exhaust pipe (10)
It is equipped on side wall stepper motor (11), and exhaust pipe (10) is internally provided with baffle (29), the baffle (29) is mounted on
In the shaft of stepper motor (11), and baffle (29) is circular configuration, and the diameter of the baffle (29) is interior with exhaust pipe (10)
Diameter diameter dimensional values are equal, and the stepper motor (11) and controller (33) are electrically connected.
5. a kind of new zeolite runner enrichment facility according to claim 3, it is characterised in that: the heat exchanger tube (22)
It is equipped on side wall intensive fin (23), the heat exchanger tube (22) is connect by second solenoid valve (24) with flue gas leading (7), institute
Second solenoid valve (24) and controller (33) are stated to be electrically connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821142570.4U CN208512201U (en) | 2018-07-16 | 2018-07-16 | A kind of new zeolite runner enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821142570.4U CN208512201U (en) | 2018-07-16 | 2018-07-16 | A kind of new zeolite runner enrichment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208512201U true CN208512201U (en) | 2019-02-19 |
Family
ID=65336178
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821142570.4U Expired - Fee Related CN208512201U (en) | 2018-07-16 | 2018-07-16 | A kind of new zeolite runner enrichment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208512201U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109985501A (en) * | 2019-04-18 | 2019-07-09 | 绍兴柯桥佳宇兴腾染整有限公司 | A kind of printing and dyeing exhaust gas three-stage processing equipment |
| CN116672849A (en) * | 2023-07-27 | 2023-09-01 | 福建路驰环境科技股份有限公司 | Organic waste gas zeolite runner integration treatment facility |
-
2018
- 2018-07-16 CN CN201821142570.4U patent/CN208512201U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109985501A (en) * | 2019-04-18 | 2019-07-09 | 绍兴柯桥佳宇兴腾染整有限公司 | A kind of printing and dyeing exhaust gas three-stage processing equipment |
| CN116672849A (en) * | 2023-07-27 | 2023-09-01 | 福建路驰环境科技股份有限公司 | Organic waste gas zeolite runner integration treatment facility |
| CN116672849B (en) * | 2023-07-27 | 2023-10-20 | 福建路驰环境科技股份有限公司 | Organic waste gas zeolite runner integration treatment facility |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190219 Termination date: 20200716 |
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| CF01 | Termination of patent right due to non-payment of annual fee |