CN112717650A - Adsorbent feeding and distributing device - Google Patents

Adsorbent feeding and distributing device Download PDF

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Publication number
CN112717650A
CN112717650A CN202011229914.7A CN202011229914A CN112717650A CN 112717650 A CN112717650 A CN 112717650A CN 202011229914 A CN202011229914 A CN 202011229914A CN 112717650 A CN112717650 A CN 112717650A
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CN
China
Prior art keywords
spray gun
shell
charging
feeding
communicated
Prior art date
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Pending
Application number
CN202011229914.7A
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Chinese (zh)
Inventor
谢新华
宋玉宝
韦振祖
宋友亚
李海斌
高英雷
周健
虢德军
赵玉水
李明磊
黄飞
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Suzhou Xire Energy Saving Environmental Protection Technology Co Ltd
Huaneng Hunan Yueyang Power Generation Co Ltd
Original Assignee
Suzhou Xire Energy Saving Environmental Protection Technology Co Ltd
Huaneng Hunan Yueyang Power Generation Co Ltd
Priority date (The priority date 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 date listed.)
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Publication date
Application filed by Suzhou Xire Energy Saving Environmental Protection Technology Co Ltd, Huaneng Hunan Yueyang Power Generation Co Ltd filed Critical Suzhou Xire Energy Saving Environmental Protection Technology Co Ltd
Priority to CN202011229914.7A priority Critical patent/CN112717650A/en
Publication of CN112717650A publication Critical patent/CN112717650A/en
Pending legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/48—Sulfur compounds
    • B01D53/50—Sulfur oxides
    • B01D53/508—Sulfur oxides by treating the gases with solids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/81—Solid phase processes
    • B01D53/83—Solid phase processes with moving reactants
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/003—Arrangements of devices for treating smoke or fumes for supplying chemicals to fumes, e.g. using injection devices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/40—Alkaline earth metal or magnesium compounds
    • B01D2251/404—Alkaline earth metal or magnesium compounds of calcium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/60—Inorganic bases or salts
    • B01D2251/602—Oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/02—Other waste gases
    • B01D2258/0283—Flue gases

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Analytical Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Nozzles (AREA)

Abstract

The invention relates to an adsorbent feeding and distributing device, which comprises a feeding unit and a mixing and distributing unit communicated with the feeding unit, wherein the feeding unit comprises a high-speed airflow supply assembly, an adsorbent supply assembly and an ejector communicated with the high-speed airflow supply assembly and the adsorbent supply assembly, and the ejector is communicated with the mixing and distributing unit; the mixing and distributing unit comprises a shell, a charging spray gun arranged in the shell and a plurality of distributing branch pipes arranged at the top of the shell, wherein the bottom of the shell is provided with a dilution air inlet; the feeding spray gun extends along the up-and-down direction of the shell, the inlet of the feeding spray gun is positioned at the top of the shell, the outlet of the feeding spray gun is positioned at the bottom of the shell, and the injector is communicated with the inlet of the feeding spray gun. The invention can meet the requirement of removing SO from basic group dry powder of the large coal-fired power plant boiler by spraying3System requirements, system reliability and economy improvementThe uniformity of dispensing is high.

Description

Adsorbent feeding and distributing device
Technical Field
The invention relates to an adsorbent feeding and distributing device.
Background
After the ultra-low emission reconstruction of the coal-fired power plant, tail facilities such as a low-low temperature economizer, wet desulphurization, a wet electric dust collector and the like can remove most of SO in the flue gas3But do not help to resolve SO3The problems of limited peak regulation depth of a unit, serious blockage of an air preheater and a low-temperature economizer by ammonium bisulfate and the like are caused. Base dry powder adsorbent is additionally arranged at inlet of SCR denitration device to remove SO by spraying3The system helps to solve the above problems.
Base dry powder adsorbent spraying to remove SO3The system belongs to a dry desulfurization technology, and the removal efficiency is directly related to the mixing effect of the flue gas and the adsorbent. In order to improve the mixing uniformity of the dry powder adsorbent and the flue gas, a plurality of spray guns are generally arranged on the flue section in a grid mode, and the flow distribution uniformity of the adsorbent of each spray gun is ensured.
See patent publication No. CN205165028U for a process for removing SO3Is dried powder mistA chemical spray device. The device comprises a dry powder storage system, a dry powder conveying system and a dry powder injection system, wherein the dry powder conveying system is connected with the injection system, base dry powder in a storage bin is blown into a distributor by high wind pressure provided by a fan to an injector, and the base dry powder enters a flue and is dispersed with SO (sulfur oxide) in the flue3And (4) reacting. The design idea is that basic group dry powder in a storage bin is blown into a distributor by high-pressure air and dispersed by the distributor and then enters a flue, the distributor is designed to insert a branch pipe into a round pipe with a larger diameter, but under the action of gravity and centrifugal force, the distribution of the dry powder adsorbent in the round pipe at the inlet of the distributor is uneven, and further the adsorbent amount in each branch pipe at the downstream is uneven; moreover, as the number of manifolds and the diameter of the distributor barrel increase, the difference in the amount of adsorbent in each manifold will further expand.
In addition, the cross-sectional dimension of the inlet and outlet flue of the SCR denitration device of the large coal-fired power plant boiler is usually 10-20 m wide and 2.5-4.5 m deep, the designed flue gas flow rate is 15 m/s, 10-40 adsorbent spray guns need to be arranged in a grid method, each spray gun is provided with one set of adsorbent metering and conveying system, the system is complex, the reliability is low, the equipment investment cost is too high, and the economical efficiency is poor. The adsorbent metering and conveying system has one used and one spare, and a plurality of spray guns are shared, so that the reliability and the economy of the system can be greatly improved, but a special feeding and distributing device needs to be developed, and the uniformity of the flow of the adsorbent of dozens of spray guns is ensured.
Disclosure of Invention
The invention aims to provide a device for feeding and distributing an adsorbent, in particular to dry powder SO3Adsorbent feeding and distributing device.
In order to achieve the purpose, the invention adopts the technical scheme that:
an adsorbent charging and dispensing device comprising a charging unit, a mixing and dispensing unit in communication with said charging unit, wherein:
the feeding unit comprises a high-speed airflow supply assembly, an adsorbent supply assembly and an ejector which is communicated with the high-speed airflow supply assembly and the adsorbent supply assembly at the same time, and the ejector is communicated with the mixing and distributing unit;
the mixing and distributing unit comprises a shell, a charging spray gun arranged in the shell, and a plurality of distributing branch pipes arranged at the top of the shell, wherein the bottom of the shell is provided with a dilution air inlet; the feeding spray gun extends along the up-and-down direction of the shell, the inlet of the feeding spray gun is positioned at the top of the shell, the outlet of the feeding spray gun is positioned at the bottom of the shell, and the injector is communicated with the inlet of the feeding spray gun.
Preferably, the mixing and distributing unit further comprises a lance tube seat and a dispersion plate, the lance tube seat is connected to the shell, and the charging lance is connected to the inside of the lance tube seat; the dispersion disc is connected to the bottom of the spray gun tube seat through a connecting rod, and the dispersion disc is over against the outlet of the charging spray gun for 10-15 mm.
Further preferably, the inner diameter of the charging spray gun is 50-80 mm, and the length of the charging spray gun is 1.5-2.0 m; the inner diameter of the gunbarrel seat is 100-120 mm.
Preferably, the mixing and distributing unit further comprises a deviation rectifying hopper connected to the outlet of the charging spray gun, and the inlet aperture of the deviation rectifying hopper is larger than the outlet aperture of the deviation rectifying hopper.
Preferably, the shell has a circular pipe section at the lower part thereof and a conical pipe section at the upper part thereof, the outlet of the charging spray gun is located at the circular pipe section, and the distribution branch pipe is located at the upper part of the conical pipe section.
Further preferably, the inner diameter of the circular pipe section is 350-450 mm, and the length of the circular pipe section is 1.5-2.5 m; the inner diameter of the top end of the conical section is 800-1200 mm, the lower cone angle is 40-70 degrees, and the upper cone angle is 140-160 degrees.
Preferably, the distribution branch pipes are uniformly distributed at the top of the shell, and the axes of the distribution branch pipes are vertical to the central line of the shell.
Preferably, the inner diameter of the distribution branch pipe is 40-60 mm.
Preferably, the high-speed air flow supply assembly comprises a blower communicated with the ejector, and a check valve, wherein the check valve is arranged on a pipeline communicated with the blower and the ejector.
Preferably, the adsorbent feeding assembly comprises a storage bin, a feeding machine and a rotary valve, wherein the feeding machine is communicated with the storage bin, the feeding machine is communicated with the ejector, and the rotary valve is arranged on a pipeline for communicating the feeding machine with the ejector.
Preferably, the feeder is a screw feeder.
Preferably, the ejector is a venturi ejector.
Preferably, the feeding units are arranged in a plurality, and the feeding units are arranged in parallel.
Due to the application of the technical scheme, compared with the prior art, the invention has the following advantages:
the invention can meet the requirement of removing SO from basic group dry powder of the large coal-fired power plant boiler by spraying3The system requirements improve the system reliability and economy and improve the distribution uniformity.
Drawings
FIG. 1 is a schematic diagram of the present embodiment;
FIG. 2 is a perspective view of the mixing and dispensing unit of this embodiment;
FIG. 3 is a side view of the mixing and dispensing unit of this embodiment;
fig. 4 is a top view of the mixing and dispensing unit of this embodiment.
In the above drawings:
10. a blower; 11. a check valve; 12. a storage bin; 13. a feeder; 14. rotating the valve; 15. an ejector; 16. a Y-shaped tee joint; 2. a mixing and dispensing unit; 20. a housing; 200. a circular pipe section; 201. a tapered tube section; 21. a lance tube holder; 22. a charging spray gun; 23. a distribution branch pipe; 24. a deviation rectifying hopper; 25. a dispersion tray; 26. a connecting rod.
Detailed Description
The technical solutions of the present invention will be described clearly and completely with reference to the accompanying drawings, and it should be understood that the described embodiments are some, but not all embodiments of the present invention. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc., indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplicity of description, but do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it should be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, e.g., as meaning either a fixed connection, a removable connection, or an integral connection; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.
The adsorbent charging and dispensing device shown in fig. 1 comprises a charging unit and a mixing and dispensing unit 2 communicated with the charging unit, and the charging unit and the mixing and dispensing unit 2 are described in detail below.
The feeding unit comprises a high-speed airflow supply assembly, an adsorbent supply assembly and an ejector 15 which is simultaneously communicated with the high-speed airflow supply assembly and the adsorbent supply assembly, and the ejector 15 is communicated with the mixing and distributing unit 2. In this embodiment:
the high-speed airflow supply assembly comprises a high-pressure blower 10 communicated with an ejector 15, a check valve 11 and a check valve 11, wherein the check valve 11 is arranged on a pipeline for communicating the blower 10 with the ejector 15; the adsorbent feeding assembly comprises a bin 12, a feeding machine 13 and a rotary valve 14, wherein the feeding machine 13 is communicated with the bin 12, the feeding machine 13 adopts a screw feeding machine and is communicated with an ejector 15, and the rotary valve 14 is arranged on a pipeline for communicating the feeding machine 13 with the ejector 15. The ejector 15 is a venturi ejector.
The feeding units may be provided in plurality, as required, in parallel, two of which are shown, one for each, for example, to improve the reliability of the system, the injectors 15 of the two feeding units being in communication with the mixing and dispensing unit 2 through a Y-shaped tee 16.
As shown in fig. 2-4: the mixing and distributing unit 2 is designed by adopting an axisymmetric structure and comprises a shell 20, a spray gun tube base 21 arranged in the shell 20, a charging spray gun 22 connected in the spray gun tube base 21, and a plurality of distributing branch pipes 23 arranged at the top of the shell 20, namely, the shell 20, the spray gun tube base 21 and the charging spray gun 22 are coaxially arranged. Specifically, the method comprises the following steps:
the bottom of the housing 20 has an inlet for dilution air. The housing 20 has a circular pipe section 200 at its lower portion and a tapered pipe section 201 at its upper portion. In this embodiment: the inner diameter of the circular pipe section 200 is 350-450 mm, and the length is 1.5-2.5 m; the inner diameter of the top end of the conical section 201 is 800-1200 mm, the lower cone angle is 40-70 degrees, and the upper cone angle is 140-160 degrees.
The spray gun tube seat 21 and the charging spray gun 22 extend along the up-down direction of the shell 20, and the spray gun tube seat 21 and the charging spray gun 22 are connected through flanges so as to facilitate the inspection, repair and replacement of the charging spray gun. The inlet of charging lance 22 is located at its top, the outlet of charging lance 22 is located at its bottom, the outlet of charging lance 22 is located in circular pipe section 200, and injector 15 is in communication with the inlet of charging lance 22. In this embodiment: the inner diameter of the nozzle tube seat 21 is 100-120 mm; the inner diameter of the charging spray gun is 50-80 mm, and the length of the charging spray gun is 1.5-2.0 m.
The mixing and distributing unit 2 further comprises a deviation rectifying hopper 24 and a dispersion plate 25. Wherein: the deviation rectifying hopper 24 is connected to the outlet of the charging spray gun 22, and the inlet caliber of the deviation rectifying hopper 24 is larger than the outlet caliber thereof and is shaped like a funnel. The dispersion disc 25 is connected to the bottom of the lance tube base 21 by connecting rods 26 (three round bars shown in the figure) and faces the outlet of the charging lance by 10-15 mm.
The distribution branch pipes 23 are uniformly distributed at the top of the shell 20, the upper part of the conical pipe section 201, and the axes of the distribution branch pipes 23 are vertical to the central line of the shell 20. In this embodiment: the inner diameter of the distribution branch pipe 23 is 40-60 mm.
The following specifically explains the working process of this embodiment:
the blower 10 works, high-pressure high-speed airflow enters the ejector 15 through the check valve 11, negative pressure is formed at a charging port at the top of the ejector 15, dry powder adsorbent falling from the rotary valve 14 above is sucked into the ejector 15, the high-speed airflow coming out of the ejector 15 carries the dry powder adsorbent to enter the mixing and distributing unit 2 through the Y-shaped tee 16, and the charging amount of the dry powder adsorbent is controlled by the rotating speed of the feeder 13; the check valve 11 and the rotary valve 14 are used for preventing the air flow and the dry powder adsorbent in the pipeline from being blown back to the blower 10 and the feeder 13. Dilution air enters from the bottom of the mixing and dispensing unit 2, mixes with the dry powder sorbent-laden air stream, and then enters each downstream sorbent injection lance from the top distribution branch 23.
In the mixing and dispensing unit 2: high-speed airflow carrying dry powder adsorbent enters the feeding spray gun 22 from the top, the airflow is fully developed in the feeding spray gun 22, the adsorbent is rectified by the rectifying hopper 24 to eliminate the problem of dry powder adherence and bias flow, the high-speed airflow carrying the dry powder adsorbent is impacted and diffused on the dispersion disc 25 after coming out of the feeding spray gun 22, the high-speed airflow is primarily mixed with dilution air flowing from bottom to top in the circular tube section 200 at the bottom of the shell 20, the flow rate of the dilution air carrying the dry powder adsorbent enters the top conical tube section 201 and is reduced, a spouting effect is formed under the action of jet flow, the mixing of the dilution air and the dry powder adsorbent is further enhanced, and the adsorbent enters each downstream adsorbent spray gun through the peripheral distribution branch tubes 23 after being uniformly mixed in the top conical tube section 201.
Example (b):
adsorbent charging and dispensing apparatus selected with the following parameters: the inner diameter of the charging spray gun 22 is 60 mm, the length of the charging spray gun is 1.7 m, the inner diameter of the spray gun tube seat 21 is 105 mm, the distance between the dispersion disc 25 and the outlet of the charging spray gun 22 is 15mm, the inner diameter of the circular tube section 200 is 350 mm, the length of the circular tube section is 1.7 m, the inner diameter of the top end of the conical tube section 201 is 1.0 m, the lower cone angle is 60 degrees, the upper cone angle is 160 degrees, and 20 distribution branch tubes 23 with the inner.
For removing SO from base dry powder by spraying3Exemplary application of the device. The physical model test adopts the calcium oxide dry powder with the grain diameter of about 325 meshes as the adsorbent, the feeding time is 30 minutes, and the test results are shown in table 1. The average adsorbent amount of 20 branches was 340g, the maximum negative deviation was-11%, the maximum positive deviation was 8%, and the relative standard deviation was 5.5%.
Table 1: and (g) the weight of the adsorbent in the outlet branch pipe of the dry powder uniform mixing and distributing device.
Branch pipe 1 Branch pipe 2 Branch pipe 3 Branch pipe 4 Branch pipe 5
313 356 333 324 329
Branch pipe 6 Branch pipe 7 Branch pipe 8 Branch pipe 9 Branch pipe 10
311 337 342 368 304
Branch pipe 11 Branch pipe 12 Branch pipe 13 Branch pipe 14 Branch pipe 15
321 339 342 357 342
Branch pipe 16 Branch pipe 17 Branch pipe 18 Branch pipe 19 Branch pipe 20
350 352 355 369 359
The above embodiments are merely illustrative of the technical ideas and features of the present invention, and the purpose thereof is to enable those skilled in the art to understand the contents of the present invention and implement the present invention, and not to limit the protection scope of the present invention. All equivalent changes and modifications made according to the spirit of the present invention should be covered within the protection scope of the present invention.

Claims (10)

1. The utility model provides a reinforced and distributor of adsorbent which characterized in that: comprises a feeding unit and a mixing and distributing unit communicated with the feeding unit, wherein:
the feeding unit comprises a high-speed airflow supply assembly, an adsorbent supply assembly and an ejector which is communicated with the high-speed airflow supply assembly and the adsorbent supply assembly at the same time, and the ejector is communicated with the mixing and distributing unit;
the mixing and distributing unit comprises a shell, a charging spray gun arranged in the shell, and a plurality of distributing branch pipes arranged at the top of the shell, wherein the bottom of the shell is provided with a dilution air inlet; the feeding spray gun extends along the up-and-down direction of the shell, the inlet of the feeding spray gun is positioned at the top of the shell, the outlet of the feeding spray gun is positioned at the bottom of the shell, and the injector is communicated with the inlet of the feeding spray gun.
2. The sorbent charging and dispensing apparatus of claim 1, wherein: the mixing and distributing unit also comprises a spray gun tube seat and a dispersion disc, wherein the spray gun tube seat is connected to the shell, and the charging spray gun is connected to the interior of the spray gun tube seat; the dispersion disc is connected to the bottom of the spray gun tube seat through a connecting rod, and the dispersion disc is over against the outlet of the charging spray gun for 10-15 mm.
3. The sorbent charging and dispensing apparatus of claim 1, wherein: the mixing and distributing unit also comprises a deviation rectifying hopper connected at the outlet of the charging spray gun, and the inlet caliber of the deviation rectifying hopper is larger than the outlet caliber of the deviation rectifying hopper.
4. The sorbent charging and dispensing apparatus of claim 1, wherein: the shell is provided with a circular pipe section at the lower part and a conical pipe section at the upper part, the outlet of the charging spray gun is positioned on the circular pipe section, and the distribution branch pipe is positioned at the upper part of the conical pipe section.
5. The sorbent charging and dispensing apparatus of claim 1, wherein: the distribution branch pipes are uniformly distributed at the top of the shell, and the axes of the distribution branch pipes are vertical to the central line of the shell.
6. The sorbent charging and dispensing apparatus of claim 1, wherein: the high-speed airflow supply assembly comprises a blower communicated with the ejector, a check valve and a pipeline, wherein the check valve is arranged on the pipeline communicated with the blower and the ejector.
7. The sorbent charging and dispensing apparatus of claim 1, wherein: the adsorbent supply assembly comprises a storage bin, a feeding machine and a rotary valve, wherein the feeding machine is communicated with the storage bin, the feeding machine is communicated with the ejector, and the rotary valve is arranged on a pipeline communicated with the feeding machine and the ejector.
8. The sorbent charging and dispensing apparatus of claim 1, wherein: the feeder is a screw feeder.
9. The sorbent charging and dispensing apparatus of claim 1, wherein: the ejector is a Venturi tube ejector.
10. The sorbent charging and dispensing apparatus of claim 1, wherein: the feeding units are arranged in a plurality and are arranged in parallel.
CN202011229914.7A 2020-11-06 2020-11-06 Adsorbent feeding and distributing device Pending CN112717650A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202011229914.7A CN112717650A (en) 2020-11-06 2020-11-06 Adsorbent feeding and distributing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202011229914.7A CN112717650A (en) 2020-11-06 2020-11-06 Adsorbent feeding and distributing device

Publications (1)

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CN112717650A true CN112717650A (en) 2021-04-30

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CN202011229914.7A Pending CN112717650A (en) 2020-11-06 2020-11-06 Adsorbent feeding and distributing device

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114307603A (en) * 2021-12-28 2022-04-12 苏州守洁环保设备有限公司 SNCR system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114307603A (en) * 2021-12-28 2022-04-12 苏州守洁环保设备有限公司 SNCR system
CN114307603B (en) * 2021-12-28 2024-02-09 苏州守洁环保设备有限公司 SNCR system

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