CN205269412U - Inactivation SCR denitration catalyst sweep device - Google Patents
Inactivation SCR denitration catalyst sweep device Download PDFInfo
- Publication number
- CN205269412U CN205269412U CN201521052416.4U CN201521052416U CN205269412U CN 205269412 U CN205269412 U CN 205269412U CN 201521052416 U CN201521052416 U CN 201521052416U CN 205269412 U CN205269412 U CN 205269412U
- Authority
- CN
- China
- Prior art keywords
- catalyst
- shock wave
- soot blower
- scr denitration
- wave soot
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/48—Liquid treating or treating in liquid phase, e.g. dissolved or suspended
- B01J38/60—Liquid treating or treating in liquid phase, e.g. dissolved or suspended using acids
-
- 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
- B01D53/96—Regeneration, reactivation or recycling of reactants
-
- 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
- B01D53/54—Nitrogen compounds
- B01D53/56—Nitrogen oxides
- B01D53/565—Nitrogen oxides by treating the gases with solids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/06—Washing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J38/00—Regeneration or reactivation of catalysts, in general
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/48—Liquid treating or treating in liquid phase, e.g. dissolved or suspended
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/48—Liquid treating or treating in liquid phase, e.g. dissolved or suspended
- B01J38/64—Liquid treating or treating in liquid phase, e.g. dissolved or suspended using alkaline material; using salts
- B01J38/66—Liquid treating or treating in liquid phase, e.g. dissolved or suspended using alkaline material; using salts using ammonia or derivatives thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Sustainable Development (AREA)
- Life Sciences & Earth Sciences (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Catalysts (AREA)
Abstract
The utility model relates to an inactivation SCR denitration catalyst sweep device should sweep the device including sweeping main part case, air compressor machine, rotatory air jetting device, shock wave soot blower and shock wave soot blower controlling means, the shock wave soot blower is used for cleaing away the deposition of inactivation SCR denitration catalyst, is located the both sides that sweep main part incasement portion, the shock wave soot blower is controlled by shock wave soot blower controlling means, just the shock wave soot blower through the pipeline with be located that to sweep the main part case outside the air compressor machine is connected, rotatory air jetting unit bit in the upper portion that sweeps main part incasement portion for jet to inactivation SCR denitration catalyst, rotatory air jetting device pass through the pipeline with the air compressor machine is connected. The utility model discloses can realize the regeneration of inactive catalyst, compare with current regeneration technology that this technology soot blowing is more thorough, the washing is more complete, and furthest resumes the surface and the pore structure of inactive catalyst.
Description
Technical field
This utility model belongs to catalyst regeneration techniques field, is specifically related to the blow device of a kind of inactivation SCR denitration catalyst.
Background technology
Industrialized develop rapidly while also exacerbate the deterioration of environment, the environmental problem such as haze is day by day serious, and along with " 12 " plan the implementation of emission reduction tasks, country's discharged nitrous oxides standard is more strict, accelerates the development of denitration technology. Due to SCR (Selectivecatalyticreduction, SCR) denitration technology mature and reliable, therefore SCR denitration technology is always in occupation of the very big market share, but catalyst cost therein is too high, and the service life of general commercial catalysts is 3-5, if directly more catalyst changeout will greatly increase its denitration cost, the waste catalyst simultaneously produced due to containing heavy metal Deng Cheng branch to environment, the regeneration issues therefore studying SCR denitration is significant.
SCR denitration is in running, due to surface area reduce, the passage of activating agent and the reason such as poisoning, catalyst activity is gradually lowered, when its activity is reduced to a certain degree, when cannot meet the needs of SCR denitration system, we term it " inactivation SCR denitration catalyst ", when this inactivation cannot reduce, we term it " discarded SCR denitration ".
Catalyst regeneration is to adopt certain technological means to make its activity obtain a degree of recovery for inactivation SCR denitration catalyst. Along with the amount of putting into operation of SCR denitration system increases, SCR denitration consumption increases, and its regeneration requirements is also increasing, has gradually formed SCR denitration regeneration market, about the ten thousand stere of domestic annual catalyst regeneration market about 20. From the viewpoint of reducing SCR denitration system operating cost and reducing discarded SCR denitration solid waste two, all need to greatly develop the regeneration industry of SCR denitration.
Utility model content
The purpose of this utility model is in that to overcome deficiency of the prior art, it is provided that the blow device purging more thorough inactivation SCR denitration catalyst of a kind of economizing type.
To achieve these goals, this utility model provides following technical scheme:
A kind of blow device of inactivation SCR denitration catalyst, this blow device includes purging main body case, air compressor machine, rotary air blowing device, shock wave soot blower and shock wave soot blower and controls device; Described shock wave soot blower is for removing the dust stratification of inactivation SCR denitration catalyst, it is positioned at the both sides purging main body case, described shock wave soot blower is controlled device by shock wave soot blower and controls, and described shock wave soot blower is connected with the described air compressor machine being positioned at outside purging main body case by pipeline; Described rotary air blowing device is positioned at the top purged within main body case, and for inactivation SCR denitration catalyst is jetted, described rotary air blowing device is connected with described air compressor machine by pipeline.
Wherein, described shock wave soot blower is n, and n is be more than or equal to 1, and this n shock wave soot blower is connected with total pipeline P0 respectively through pipeline P1 ..., Pn, it is connected with described air compressor machine by described total pipeline P0, described pipeline P1 ..., Pn are respectively provided with air inlet stop valve; It is 1 that this shock wave soot blower controls device, arranges different control knobs for every shock wave soot blower.
Wherein, the quantity of described shock wave soot blower is four, is separately positioned on purging both sides, middle part within main body case and both sides, top.
Wherein, the pipeline that rotary air blowing device is connected with air compressor machine arranges persevering airflow apparatus, or is additionally provided with stop valve, air inlet adjustment valve and Pressure gauge.
Wherein, the bottom within described purging main body case is provided with flue-dust retainer, is provided with, at the box bottom purging main body case, the ash hole being connected with described flue-dust retainer.
Further, described inactivation SCR denitration catalyst is placed in described flue-dust retainer top by net-shaped steel structure.
The beneficial effects of the utility model are:
The blow device of a kind of inactivation SCR denitration catalyst disclosed in this utility model, compared with existing blow device, this utility model adopts shock-wave ash blowing and rotary air to purge the mode combined, can loose obstinate dust, soot blowing intensity is high, soot blowing is more thorough, cleaning, it is possible to effectively removes the dust adhered on a catalyst, farthest recovers surface and the pore structure of inactivation SCR denitration catalyst. .
The blow device that additionally this utility model adopts can also collect dust effectively, reduces flying dust.
Accompanying drawing explanation
The preferred process chart of Fig. 1 one of the present utility model;
Fig. 2 blow device structure chart of the present utility model;
Fig. 3 airtight rinser structure chart of the present utility model;
Fig. 4 semidry method ultrasonic activation structure drawing of device of the present utility model;
The structural representation of the regenerative system of Fig. 5 inactivation SCR denitration catalyst of the present utility model.
Wherein, 1 cleans main body case, 11 acid entrances, 12 deionized water entrances, 13 liquid outlets, 2 soniclizeies, 21 excusing from death atomized liquid nozzles, 3 supersonic cleaning machines, 4 microbubble generators, 41 air pumps, 5 catalyst wash rotating disks, 51 motors, 6 Regenrable catalyzed doses, 7 tiny structure aspirators
8 purging main body cases, 9 air compressor machines, 10 permanent airflow apparatus, 14 stop valves, 15 adjustment valves, 16 Pressure gauges, 17 rotary air blowing devices, 18 shock wave soot blowers control devices, 19 shock wave soot blowers, 20 stop valves, 22 ash holes, 23 flue-dust retainers, 24 Regenrable catalyzed doses
32 soniclizeies, 33 regeneration main body cases, 34 regeneration liquid waste outlets, 35 atomized liquid nozzles, 36 catalyst rotary turnplate, 38 motors, 39 tiny structure aspirators
Detailed description of the invention
[related definition]
" inactivation SCR denitration catalyst " described in the utility model refers to, SCR denitration is in running, due to catalyst dust stratification, active component passage and the reason such as active sites is poisoning, catalyst activity is gradually lowered, when its activity is reduced to the needs that cannot meet SCR denitration system, just it is referred to as " inactivation SCR denitration catalyst ". Specifically, SCR denitration there will be inactivation after properly functioning certain time, and its reason mainly has:
A. alkali metal, alkaline-earth metal, heavy metal etc. make the quantity of catalyst surface acidic site and intensity reduce;
B. the blocking catalyst duct such as flue gas flying dust, sulfur ammonium salt;
C. long-lasting catalytic runs and causes sintering of catalyst, etc.
Wherein, reason a, b the decaying catalyst caused, belong to the reproducible inactivation SCR denitration catalyst alleged by this utility model, also referred to as inactivation SCR denitration catalyst or Regenrable catalyzed dose.
The known SCR denitration used in described SCR denitration and prior art.
The parts contacted with water or acid in this utility model all adopt corrosion-resistant, acidproof material, or adopt corrosion-resistant, acidproof material to be coated with.
[blow device and blowing method]
As it was previously stated, this utility model provides the blow device of a kind of inactivation SCR denitration catalyst. As in figure 2 it is shown, blow device of the present utility model includes purging main body case 8, air compressor machine 9, rotary air blowing device 17, shock wave soot blower 19 and shock wave soot blower controls device 18.
Described rotary air blowing device 17 is positioned at the top purged within main body case 8, and is connected with outside air compressor machine 9 by pipeline; This pipeline can be arranged as required to permanent airflow apparatus 10, stop valve 14, air inlet adjustment valve 15 and Pressure gauge 16 etc.
Described shock wave soot blower 19 is for removing the dust stratification of inactivation SCR denitration catalyst, and its quantity can be arranged according to practical situation. Fig. 2 illustrates the situation of four shock wave soot blowers, position and the annexation of shock wave soot blower have been described for these four shock wave soot blowers below.
These four shock wave soot blowers are separately positioned on purging both sides, middle part within main body case and both sides, top, all shock wave soot blowers control device 18 by same shock wave soot blower and control, four shock wave soot blowers are connected respectively through pipeline P1, P2, P3 and P4 and one total pipeline P0, and described shock wave soot blower is connected with above-mentioned air compressor machine 9 by main pipe rail P0. Every shock wave soot blower realizes starting by the different control knob on described control device 18, carries out shock-wave ash blowing. Described pipeline P1, P2, P3 and P4 can also be respectively provided with valve (such as air inlet stop valve) 20, realized the Stress control in shock wave soot blower by this valve and air compressor machine.
Bottom within described purging main body case 8 is provided with flue-dust retainer 23, is provided with, at the box bottom purging main body case 8, the ash hole 22 being connected with described flue-dust retainer 23, and inactivation SCR denitration catalyst 24 is placed in described flue-dust retainer top by net-shaped steel structure.
Wherein, during work, inactivation SCR denitration catalyst is placed in purging main body case 8 (such as described inactivation SCR denitration catalyst is placed in described flue-dust retainer top by net-shaped steel structure), start air compressor machine 9, open the air inlet stop valve 20 entering shock wave soot blower, observe shock wave soot blower and control the Pressure gauge of device, after pressure is suitable (such as 0.8-1.2MPa), the soot blower being controlled both sides, device startup middle part by shock wave soot blower is purged 2-5 time, and the shock wave soot blower restarting both sides, top purges 3-5 time; After shock-wave ash blowing terminates, close shock wave soot blower, simultaneously close off the air inlet adjustment valve 20 on the P1 of shock wave soot blower, P2, P3 and P4. Opening the air inlet adjustment valve 15 of rotary air blowing device 17, regulate pressure to 0.4-0.6MPa with air compressor machine, purge 5-10min by rotary air blowing device 17, flying dust is collected in flue-dust retainer, and can be discharged by ash hole.
[rinser and cleaning method]
This utility model also proposed the airtight rinser of a kind of inactivation SCR denitration catalyst, as it is shown on figure 3, the airtight rinser of inactivation SCR denitration catalyst of the present utility model includes cleaning main body case 1, soniclizer 2, supersonic cleaning machine 3, microbubble generator 4, catalyst wash rotating disk 5 and tiny structure aspirator 7. Ultrasound wave conductive plate is separated into upper and lower by internal for cleaning main body case 1, soniclizer 2 and catalyst wash rotating disk 5 are arranged on the top cleaning main body case 1, supersonic cleaning machine 3 and microbubble generator 4 are arranged on the bottom cleaning main body case 1, and tiny structure aspirator 7 is arranged on the casing cleaning main body case 1 top. Wherein, soniclizer 2 is arranged on the upper area cleaning main body case 1 top, and soniclizer 2 is arranged below ultrasonic atomizatio nozzle for liquid 21, by ultrasonic atomizatio nozzle for liquid 21 to cleaning the cleanout fluid spraying ultrasonic atomization in main body case 1; Catalyst wash rotating disk 5 is used for placing catalyst 6, catalyst wash rotating disk 5 and catalyst 6 and is respectively positioned on below ultrasonic atomizatio nozzle for liquid 21; Catalyst wash rotating disk 5 is installed below motor 51; Tiny structure aspirator 7 is positioned at above catalyst wash rotating disk 5 and catalyst 6; Microbubble generator 4 is combined air pump 41 and is produced microbubble, by pipeline, microbubble is externally introduced, from cleaning main body case 1 bottom, the position cleaning main body case 1 top higher than catalyst 6 via cleaning main body case 1, it is incorporated near motor 51 again through pipeline, for catalyst 6 is carried out; The casing side cleaning main body case 1 top is provided with acid entrance 11 and deionized water entrance 12, opposite side is provided with liquid outlet 13, acid entrance 11 and deionized water entrance 12 are lower than the position of catalyst 6, and liquid outlet 13 is positioned at the bottom cleaning main body case 1 top, it is simple to discharge acid solution or deionized water; Alternatively, deionized water entrance 12 can also be arranged on liquid outlet 13 side.
Shown in some processes flow process in the technological process of this rinser such as Fig. 1. During work, inactivation SCR denitration catalyst 6 is placed in above catalyst wash rotating disk 5, and under the driving of motor 51, catalyst wash rotating disk 5 drives described catalyst 6 to rotate; First pass through described microbubble generator 4 and produce microbubble by air pump 41, impact ablution with microbubble explosion and clean described catalyst 6, after having cleaned, close air pump 41; Then pass through tiny structure aspirator 7 and be internally formed tiny structure environment at cleaning main body case 1; Under tiny structure environment, sprayed the cleanout fluid of ultrasonic atomization with soniclizer 2 by ultrasonic atomizatio nozzle for liquid 21, clean described catalyst 6 with semidry method, after having cleaned, close soniclizer 2; Opening after acid entrance 11 passes into appropriate acid solution again and close acid entrance 11, described supersonic cleaning machine 3 cleans described catalyst 6 with acid dip under ultrasound condition, after having impregnated, discharges acid solution by liquid outlet 13; Finally opening deionized water entrance 12 and pass into deionized water, described supersonic cleaning machine 3 washs described catalyst 6 by flow deionized water under ultrasound condition, and the deionized water after washing is discharged by liquid outlet 13, closes deionized water entrance 12 after having washed.
The cleaning method of a kind of inactivation SCR denitration catalyst is also provided at this utility model, it adopts above-mentioned airtight rinser, its processing step includes: described inactivation SCR denitration catalyst be placed on the catalyst wash rotating disk of described airtight rinser, impact ablution by described microbubble generator with microbubble explosion to clean, then clean with semidry method with soniclizer under tiny structure environment, clean with acid dip under ultrasound condition again through described supersonic cleaning machine, finally wash by flow deionized water again.
Wherein, first carry out microbubble explosion and impact cleaning 10-50min, then under tiny structure environment, clean 10-50min with soniclizer with semidry method, then clean 5-10min with acid dip under ultrasound condition, finally wash 3-5min by flow deionized water again.
Wherein, the described time cleaned with microbubble explosion impact ablution is for 10-50min, it is preferable that 20-30min. Specifically, described is under ultrasound condition with microbubble explosion impact cleaning, and with cleaning 10-50min under microbubble generator and air pump synergy, its supersonic frequency is 30KHz-40KHz, and the flow of air pump is 0.4m3/h-0.8m3/h��
Wherein, with soniclizer with time that semidry method is cleaned for 10-50min, it is preferable that 20-30min. Specifically, described semidry method is cleaned and is: described tiny structure aspirator is internally formed tiny structure environment at cleaning main body case; Soniclizer, under tiny structure environment, cleans 10-50min with the micron order mist particles cleanout fluid that clean air is carrier gas, and wherein the condensation rate of soniclizer is 0.05L/min-1L/min, and flow rate of carrier gas is 0.1m3/h-5m3/ h, soniclizer frequency is 1.0MHz-4.5MHz.
Wherein, the time cleaned with acid dip is 5-10min.
Wherein, the time with flow deionized water washing is 3-5min.
[activation device and activation method]
As it was previously stated, this utility model provides the activation device of a kind of inactivation SCR denitration catalyst. As shown in Figure 4, described activation device includes regeneration main body case 33, soniclizer 32, catalyst rotary turnplate 36 and tiny structure aspirator 39, soniclizer 32 and catalyst rotary turnplate 36 are arranged on the box house of regeneration main body case 33, tiny structure aspirator 39 is arranged on the casing of regeneration main body case 33, wherein soniclizer 32 is arranged on the top of regeneration main body case 33, and soniclizer 32 is arranged below ultrasonic atomizatio nozzle for liquid 35; Catalyst rotary turnplate 36 is positioned at the middle part of regeneration main body case 33; The casing side of regeneration main body case 33 is provided with regeneration liquid waste outlet 34.
During work, inactivation SCR denitration catalyst to be activated is placed in above catalyst rotary turnplate 36, and under the driving of motor 38, catalyst rotary turnplate 36 drives described catalyst to rotate. Described tiny structure aspirator 39 is internally formed tiny structure environment at regeneration main body case 33; Soniclizer 32 sprays the micron order mist particles regeneration activity liquid of the ultrasonic atomization being carrier gas with clean air under tiny structure environment by ultrasonic atomizatio nozzle for liquid 35 to described catalyst, with catalyst described in semidry method regeneration activating. Wherein, described regeneration activity liquid is made up of penetrating agent, surfactant, chelating agent, regeneration activity composition ammonium metavanadate, active component auxiliary agent, acid and deionized water. Its formula and consumption can configure according to practical situation. Wherein, penetrating agent is selected from penetrating agent JFC; Surfactant is selected from OP-10; Chelating agent is selected from polyvinyl alcohol or triethanolamine; Active component auxiliary agent is selected from ammonium paratungstate; Acid is one or more in oxalic acid, acetic acid or carbonic acid.
[regenerative system and renovation process]
This utility model additionally provides the regenerative system of a kind of inactivation SCR denitration catalyst, described regenerative system includes the blow device, rinser, the first drying device and the activation device that are sequentially connected with, and wherein inactivation SCR denitration catalyst is purged by blow device; Catalyst after blow device purges is carried out by rinser; Catalyst after the cleaning of cleaned device is dried by described first drying device; Dried catalyst is carried out regeneration activating process by described activation device.
Wherein, described blow device is above-mentioned blow device of the present utility model.
Wherein, described rinser is above-mentioned of the present utility model airtight rinser.
Wherein, described activation device is above-mentioned activation device of the present utility model.
Wherein, described blow device is above-mentioned blow device of the present utility model, and described rinser is above-mentioned of the present utility model airtight rinser.
Wherein, described blow device is above-mentioned blow device of the present utility model, and described activation device is above-mentioned activation device of the present utility model.
Wherein, described rinser is above-mentioned of the present utility model airtight rinser, and described activation device is above-mentioned activation device of the present utility model.
Wherein, described blow device is above-mentioned blow device of the present utility model, and described rinser is above-mentioned of the present utility model airtight rinser, and described activation device is above-mentioned activation device of the present utility model.
Wherein, after described activation device, also include the second drying device, described second drying device activated device is processed after catalyst be dried, roasting and cooling process.
Wherein, described first drying device or the second drying device are baking oven or catalyst drying machine.
Wherein, described activation device is regeneration activity load device.
As it is shown in figure 1, this utility model also provides for the renovation process of a kind of inactivation SCR denitration catalyst, it adopts above-mentioned regenerative system; The processing step of described renovation process includes:
(1) inactivation SCR denitration catalyst is placed in blow device, purges;
(2) catalyst after step (1) processes is placed in rinser, is carried out;
(3) it is dried in described first drying device through the catalyst that step (2) is cleaned;
(4) it is placed in regeneration in activation device through the catalyst that step (3) is dried.
Wherein, described method further includes steps of
(5) catalyst regenerated through step (4) dry, roasting in the second drying device, cooling are obtained the SCR denitration of regeneration.
Wherein, in step (1), adopting clean air to purge, pressure is 0.4-0.6MPa, and the time is 10-20min.
Wherein, in step (2), airtight rinser of the present utility model is adopted to clean, including following four steps: cleaning, semidry method cleaning, acid dip cleaning and running water are impacted in microbubble explosion.
Wherein, in step (2), first carry out microbubble explosion and impact cleaning 10-50min (preferred 20-30min), then under tiny structure environment, 10-50min (preferred 20-30min) is cleaned with soniclizer with semidry method, under ultrasound condition, clean 5-10min with acid dip again, finally wash 3-5min by flow deionized water again.
Wherein, it is under ultrasound condition that cleaning is impacted in microbubble explosion in step (2), with cleaning 10-50min (preferred 20-30min) under microbubble generator and air pump synergy, its supersonic frequency is 30KHz-40KHz, and the flow of air pump is 0.4m3/h-0.8m3/h��
Wherein, the semidry method in step (2) is cleaned and is: described tiny structure aspirator is internally formed tiny structure environment at cleaning main body case; Soniclizer, under tiny structure environment, cleans 10-50min (preferred 20-30min) with the micron order mist particles cleanout fluid that clean air is carrier gas, and wherein the condensation rate of ultrasound atomizer is 0.05L/min-1L/min, and flow rate of carrier gas is 0.1m3/h-5m3/ h, ultrasound atomizer frequency is 1.0MHz-4.5MHz.
This utility model impacts cleaning in conjunction with microbubble explosion, and its advantage is the surface and the micropore that utilize the produced surface of microbubble explosion can impact catalyst, peels off the dust of absorption, thus reaching cleaning performance.
Wherein, in step (3), dry 3-5h at 80-110 DEG C.
Wherein, in step (4), described activation device is regeneration activity load device, is obtained the catalyst of regeneration activity liquid load by described device.
Wherein, in step (4), described activation device is activation device of the present utility model, is obtained the catalyst of regeneration activity liquid load by described device.
Wherein, in step (5), will through the catalyst of (4) regeneration activity liquid load dry 4-6h, then roasting 4-6h at 400-600 DEG C at 80-120 DEG C of temperature, cooling obtains the SCR denitration of regeneration.
This utility model utilizes micron order atomization cleaning liquid that catalyst is carried out, and its advantage can farthest recover surface and the pore structure of inactivation SCR denitration catalyst while of being and improve cleanout fluid utilization rate.
This utility model utilizes micron order atomization regeneration activity liquid that catalyst is activated, and its advantage can farthest recover surface and the pore structure of described inactivation SCR denitration catalyst while of being and improve regeneration activity liquid utilization rate.
Below by way of specific embodiment, the utility model is described in further detail, but this should not being interpreted as, scope of the present utility model is only limitted to Examples below. When without departing from this utility model said method thought, the various replacements made according to ordinary skill knowledge and customary means or change, should be included in scope of the present utility model.
In following example raw materials used if no special instructions, be all the commercial product well known by persons skilled in the art that can be commercially available.
The regeneration activity liquid used in following embodiment is the existing active liquid for SCR denitration regeneration in prior art, is made up of penetrating agent, surfactant, chelating agent, regeneration activity composition ammonium metavanadate, active component auxiliary agent, acid and deionized water. Its formula and consumption can configure according to practical situation. Wherein, penetrating agent is selected from penetrating agent JFC; Surfactant is selected from OP-10; Chelating agent is selected from polyvinyl alcohol or triethanolamine; Active component auxiliary agent is selected from ammonium paratungstate; Acid is one or more in oxalic acid, acetic acid or carbonic acid.
Embodiment 1-1
Realize through the method and system shown in Fig. 1-5 that denitration activity reduces to 18Nm/h, specific surface area reduces to 41.2m2The Regeneration Treatment of the catalyst (being designated as decaying catalyst A) of/g:
(1) decaying catalyst A is placed in the blow device shown in Fig. 2 purges with shock wave soot blower, shock-wave ash blowing number of times be 7 times (wherein, the soot blowing of both sides, middle part 4 times, the soot blowing of both sides, top 3 times), soot blowing dead angle is few, can dispel out by obstinate dust, then purges 20min with the clean air that pressure is 0.55MPa again;
(2) catalyst after (1) being processed is placed in the airtight rinser shown in Fig. 3, and with microbubble explosion impact ablution cleaning 22min, (wherein, supersonic frequency is 35KHz, and the flow of air pump is 0.6m3/ h), (wherein, the condensation rate of soniclizer is 0.3L/min, and flow rate of carrier gas is 2.5m then to clean 26min with soniclizer with semidry method under tiny structure environment3/ h, soniclizer frequency is 2.5MHz), then clean 6min with acid dip under ultrasound condition, finally wash 4.5min by flow deionized water again;
(3) by catalyst cleaned to (2) 90 DEG C of dry 3h in the first drying device;
(4) catalyst dried to (3) is placed in the activation device shown in Fig. 4, it is atomized regeneration activity liquid ultrasonic spray regeneration activity liquid (wherein with semidry method micron order, the condensation rate of soniclizer is 0.3L/min, and flow rate of carrier gas is 2.5m3/ h, soniclizer frequency is 2.5MHz) regenerate 3h;
(5) catalyst through regeneration activity liquid load drying 4h, then roasting 4.5h at 450 DEG C in the second drying device at 105 DEG C of temperature, cooling obtains the SCR denitration of regeneration.
Being placed in SCR denitration activity test unit by the SCR denitration after Regeneration Treatment, test denitration efficiency and detect its specific surface area under simulated flue gas, regenerated outcome is following table 1-1 such as:
Table 1-1
Embodiment 1-2
Realize through the method and system shown in Fig. 1-5 that denitration activity reduces to 18Nm/h, specific surface area reduces to 41.2m2The Regeneration Treatment of the catalyst (being designated as decaying catalyst A) of/g:
(1) decaying catalyst A is placed in the blow device shown in Fig. 1 purges with shock wave soot blower, shock-wave ash blowing number of times be 7 times (wherein, the soot blowing of both sides, middle part 4 times, the soot blowing of both sides, top 3 times), then purge 20min with the clean air that pressure is 0.55MPa again;
(2) catalyst after (1) being processed is placed in rinser ultrasonic cleaning 20-50min;
(3) by catalyst cleaned to (2) 90 DEG C of dry 3h in the first drying device;
(4) catalyst dried to (3) is placed in known active device, regenerates 3h with regeneration activity liquid;
(5) catalyst through regeneration activity liquid load drying 4h, then roasting 4.5h at 450 DEG C in the second drying device at 105 DEG C of temperature, cooling obtains the SCR denitration of regeneration.
Being placed in SCR denitration activity test unit by the SCR denitration after Regeneration Treatment, test denitration efficiency and detect its specific surface area under simulated flue gas, regenerated outcome is following table 1-2 such as:
Table 1-2
Embodiment 2
Realize through the method and system shown in Fig. 1-5 that denitration activity reduces to 25Nm/h, specific surface area reduces to 37.8m2The Regeneration Treatment of the catalyst (being designated as decaying catalyst B) of/g:
(1) decaying catalyst B is placed in the blow device shown in Fig. 2 purges with shock wave soot blower, shock-wave ash blowing number of times be 8 times (wherein, the soot blowing of both sides, middle part 4 times, the soot blowing of both sides, top 4 times), soot blowing dead angle is few, can dispel out by obstinate dust, then purges 15min with the clean air that pressure is 0.45MPa again;
(2) catalyst after (1) being processed is placed in the airtight rinser shown in Fig. 3, and with microbubble explosion impact ablution cleaning 20min, (wherein, supersonic frequency is 35KHz, and the flow of air pump is 0.5m3/ h), (wherein, the condensation rate of soniclizer is 0.1L/min, and flow rate of carrier gas is 1.5m then to clean 25min with soniclizer with semidry method under tiny structure environment3/ h, soniclizer frequency is 4.0MHz), then wash 7min with acid dip under ultrasound condition, finally washing 3.5min by flow deionized water;
(3) catalyst cleaned to (2) is dried in the first drying device 3h at 110 DEG C;
(4) catalyst dried to (3) is placed in the activation device shown in Fig. 4, it is atomized regeneration activity liquid ultrasonic spray regeneration activity liquid (wherein with semidry method micron order, the condensation rate of soniclizer is 0.8L/min, and flow rate of carrier gas is 2.5m3/ h, soniclizer frequency is 2MHz) regenerate 2.5h;
(5) catalyst through regeneration activity liquid load drying 4.5h, then roasting 4h at 550 DEG C in the second drying device at 100 DEG C of temperature, cooling obtains the SCR denitration of regeneration.
Being placed in SCR denitration activity test unit by the SCR denitration after Regeneration Treatment, test regeneration catalyzing agent performance and detect its specific surface area under simulated flue gas, regenerated outcome is table 2 below such as:
Table 2
Embodiment 3-1
Realize through the method and system shown in Fig. 1-5 that denitration activity reduces to 20Nm/h, specific surface area reduces to 45.4m2The Regeneration Treatment of the catalyst (being designated as decaying catalyst C) of/g:
(1) decaying catalyst C is placed in the blow device shown in Fig. 2 and purges with shock wave soot blower, shock-wave ash blowing number of times be 10 times (wherein, the soot blowing of both sides, middle part 5 times, the soot blowing of both sides, top 5 times);
(2) catalyst after (1) being processed is placed in the airtight rinser shown in Fig. 3, and with microbubble explosion impact ablution cleaning 20min, (wherein, supersonic frequency is 35KHz, and the flow of air pump is 0.7m3/ h), (wherein, the condensation rate of soniclizer is 0.9L/min, and flow rate of carrier gas is 4.5m then to clean 20min with soniclizer with semidry method under tiny structure environment3/ h, soniclizer frequency is 1.0MHz), then clean 10min with acid dip under ultrasound condition, finally washing 5min by flow deionized water;
(3) catalyst cleaned to (2) is dried in the first drying device 5h at 100 DEG C;
(4) catalyst dried to (3) is placed in the activation device shown in Fig. 4, it is atomized regeneration activity liquid ultrasonic spray regeneration activity liquid (wherein with semidry method micron order, the condensation rate of soniclizer is 0.5L/min, and flow rate of carrier gas is 2m3/ h, soniclizer frequency is 3MHz) regenerate 2h;
(5) catalyst through regeneration activity liquid load drying 5h, then roasting 4h at 500 DEG C in the second drying device at 110 DEG C of temperature, cooling obtains the SCR denitration of regeneration.
SCR denitration after Regeneration Treatment is placed in SCR denitration activity test unit, test regeneration denitrating catalyst performance and its specific surface area of detection under simulated flue gas, regenerated outcome is following table 3-1 such as:
Table 3-1
Embodiment 3-2
Realize through the method and system shown in Fig. 1-5 that denitration activity reduces to 20Nm/h, specific surface area reduces to 45.4m2The Regeneration Treatment of the catalyst (being designated as decaying catalyst C) of/g:
(1) decaying catalyst C is placed in blow device and purges 15min with the clean air that pressure is 0.4MPa;
(2) catalyst after (1) being processed is placed in the airtight rinser shown in Fig. 3, and with microbubble explosion impact ablution cleaning 20min, (wherein, supersonic frequency is 35KHz, and the flow of air pump is 0.7m3/ h), (wherein, the condensation rate of soniclizer is 0.9L/min, and flow rate of carrier gas is 4.5m then to clean 20min with soniclizer with semidry method under tiny structure environment3/ h, soniclizer frequency is 1.0MHz), then clean 10min with acid dip under ultrasound condition, finally washing 5min by flow deionized water;
(3) catalyst cleaned to (2) is dried in the first drying device 5h at 100 DEG C;
(4) catalyst dried to (3) is placed in the activation device shown in Fig. 4, it is atomized regeneration activity liquid ultrasonic spray regeneration activity liquid (wherein with semidry method micron order, the condensation rate of soniclizer is 0.5L/min, and flow rate of carrier gas is 2m3/ h, soniclizer frequency is 3MHz) regenerate 2h;
(5) catalyst through regeneration activity liquid load drying 5h, then roasting 4h at 500 DEG C in the second drying device at 110 DEG C of temperature, cooling obtains the SCR denitration of regeneration.
SCR denitration after Regeneration Treatment is placed in SCR denitration activity test unit, test regeneration denitrating catalyst performance and its specific surface area of detection under simulated flue gas, regenerated outcome is following table 3-2 such as:
Table 3-2
Embodiment 3-3
Realize through the method and system shown in Fig. 1-5 that denitration activity reduces to 20Nm/h, specific surface area reduces to 45.4m2The Regeneration Treatment of the catalyst (being designated as decaying catalyst C) of/g:
(1) decaying catalyst C is placed in the blow device shown in Fig. 2 purges with shock wave soot blower, shock-wave ash blowing number of times be 10 times (wherein, the soot blowing of both sides, middle part 5 times, the soot blowing of both sides, top 5 times), then purge 15min with the clean air that pressure is 0.4MPa again;
(2) catalyst after (1) being processed is placed in the airtight rinser shown in Fig. 3, and with microbubble explosion impact ablution cleaning 20min, (wherein, supersonic frequency is 35KHz, and the flow of air pump is 0.7m3/ h), (wherein, the condensation rate of soniclizer is 0.9L/min, and flow rate of carrier gas is 4.5m then to clean 20min with soniclizer with semidry method under tiny structure environment3/ h, soniclizer frequency is 1.0MHz), then clean 10min with acid dip under ultrasound condition, finally washing 5min by flow deionized water;
(3) catalyst cleaned to (2) is dried in the first drying device 5h at 100 DEG C;
(4) catalyst dried to (3) is placed in the activation device shown in Fig. 4, it is atomized regeneration activity liquid ultrasonic spray regeneration activity liquid (wherein with semidry method micron order, the condensation rate of soniclizer is 0.5L/min, and flow rate of carrier gas is 2m3/ h, soniclizer frequency is 3MHz) regenerate 2h;
(5) catalyst through regeneration activity liquid load drying 5h, then roasting 4h at 500 DEG C in the second drying device at 110 DEG C of temperature, cooling obtains the SCR denitration of regeneration.
SCR denitration after Regeneration Treatment is placed in SCR denitration activity test unit, test regeneration denitrating catalyst performance and its specific surface area of detection under simulated flue gas, regenerated outcome is following table 3-3 such as:
Table 3-3
Embodiment 4
Realize through the method and system shown in Fig. 1-2,4-5 that denitration activity reduces to 18Nm/h, specific surface area reduces to 41.2m2The Regeneration Treatment of the catalyst (being designated as decaying catalyst A) of/g:
(1) decaying catalyst A is placed in the blow device shown in Fig. 2 purges with shock wave soot blower, shock-wave ash blowing number of times be 7 times (wherein, the soot blowing of both sides, middle part 4 times, the soot blowing of both sides, top 3 times), then purge 20min with the clean air that pressure is 0.55MPa again;
(2) catalyst after (1) being processed is placed in the airtight rinser shown in Fig. 3, and with microbubble explosion impact ablution cleaning 22min, (wherein, supersonic frequency is 35KHz, and the flow of air pump is 0.6m3/ h), (wherein, the condensation rate of soniclizer is 0.3L/min, and flow rate of carrier gas is 2.5m then to clean 26min with soniclizer with semidry method under tiny structure environment3/ h, soniclizer frequency is 2.5MHz), then clean 6min with acid dip under ultrasound condition, finally washing 4.5min by flow deionized water;
(3) by catalyst cleaned to (2) 90 DEG C of dry 3h in the first drying device;
(4) catalyst dried to (3) is placed in known active device, regenerates 3h with regeneration activity liquid;
(5) catalyst through regeneration activity liquid load drying 4h, then roasting 4.5h at 450 DEG C in the second drying device at 105 DEG C of temperature, cooling obtains the SCR denitration of regeneration.
Being placed in SCR denitration activity test unit by the SCR denitration after Regeneration Treatment, test denitration efficiency and detect its specific surface area under simulated flue gas, regenerated outcome is table 4 below such as:
Table 4
Embodiment 5
Realize through Fig. 1-3, the method and system shown in 5 that denitration activity reduces to 25Nm/h, specific surface area reduces to 37.8m2The Regeneration Treatment of the catalyst (being designated as decaying catalyst B) of/g:
(1) decaying catalyst B is placed in purging pond and purges 15min with the clean air that pressure is 0.45MPa;
(2) catalyst after (1) being processed is placed in the airtight rinser shown in Fig. 3, and with microbubble explosion impact ablution cleaning 20min, (wherein, supersonic frequency is 35KHz, and the flow of air pump is 0.5m3/ h), (wherein, the condensation rate of soniclizer is 0.1L/min, and flow rate of carrier gas is 1.5m then to clean 25min with soniclizer with semidry method under tiny structure environment3/ h, soniclizer frequency is 4.0MHz), then wash 7min with acid dip under ultrasound condition, finally washing 3.5min by flow deionized water;
(3) catalyst cleaned to (2) is dried in the first drying device 3h at 110 DEG C;
(4) catalyst dried to (3) is placed in the activation device shown in Fig. 4, it is atomized regeneration activity liquid ultrasonic spray regeneration activity liquid (wherein with semidry method micron order, the condensation rate of soniclizer is 0.8L/min, and flow rate of carrier gas is 2.5m3/ h, soniclizer frequency is 2MHz) regenerate 2.5h;
(5) catalyst through regeneration activity liquid load drying 4.5h, then roasting 4h at 550 DEG C in the second drying device at 100 DEG C of temperature, cooling obtains the SCR denitration of regeneration.
Being placed in SCR denitration activity test unit by the SCR denitration after Regeneration Treatment, test regeneration catalyzing agent performance and detect its specific surface area under simulated flue gas, regenerated outcome is table 5 below such as:
Table 5
Embodiment 6
Realize through the method and system shown in Fig. 1,3-5 that denitration activity reduces to 20Nm/h, specific surface area reduces to 45.4m2The Regeneration Treatment of the catalyst (being designated as decaying catalyst C) of/g:
(1) decaying catalyst C is placed in the blow device shown in Fig. 2 purges with shock wave soot blower, shock-wave ash blowing number of times be 10 times (wherein, the soot blowing of both sides, middle part 5 times, the soot blowing of both sides, top 5 times), then purge 15min with the clean air that pressure is 0.4MPa again;
(2) catalyst after (1) being processed is placed in rinser ultrasonic cleaning 20-50min;
(3) catalyst cleaned to (2) is dried in the first drying device 5h at 100 DEG C;
(4) catalyst dried to (3) is placed in the activation device shown in Fig. 4, it is atomized regeneration activity liquid ultrasonic spray regeneration activity liquid (wherein with semidry method micron order, the condensation rate of soniclizer is 0.5L/min, and flow rate of carrier gas is 2m3/ h, soniclizer frequency is 3MHz) regenerate 2h;
(5) catalyst through regeneration activity liquid load drying 5h, then roasting 4h at 500 DEG C in the second drying device at 110 DEG C of temperature, cooling obtains the SCR denitration of regeneration.
SCR denitration after Regeneration Treatment is placed in SCR denitration activity test unit, test regeneration denitrating catalyst performance and its specific surface area of detection under simulated flue gas, regenerated outcome is table 6 below such as:
Table 6
Claims (7)
1. the blow device of an inactivation SCR denitration catalyst, it is characterised in that this blow device includes purging main body case, air compressor machine, rotary air blowing device, shock wave soot blower and shock wave soot blower and controls device; Described shock wave soot blower is for removing the dust stratification of inactivation SCR denitration catalyst, it is positioned at the both sides purged within main body case, described shock wave soot blower is controlled device by shock wave soot blower and controls, and described shock wave soot blower is connected with the described air compressor machine being positioned at outside purging main body case by pipeline; Described rotary air blowing device is positioned at the top purged within main body case, and for inactivation SCR denitration catalyst is jetted, described rotary air blowing device is connected with described air compressor machine by pipeline.
2. blow device according to claim 1, it is characterized in that, described shock wave soot blower is n, n is be more than or equal to 1, this n shock wave soot blower is connected with total pipeline P0 respectively through pipeline P1 ..., Pn, it is connected with described air compressor machine by described total pipeline P0, described pipeline P1 ..., Pn are respectively provided with air inlet stop valve; It is 1 that this shock wave soot blower controls device, arranges different control knobs for every shock wave soot blower.
3. blow device according to claim 2, it is characterised in that the quantity of described shock wave soot blower is four, is respectively arranged at purging both sides, middle part within main body case and both sides, top.
4. blow device according to claim 1, it is characterised in that persevering airflow apparatus is set on the pipeline that rotary air blowing device is connected with air compressor machine.
5. blow device according to claim 4, it is characterised in that be additionally provided with stop valve, air inlet adjustment valve and Pressure gauge with air compressor machine on the pipeline that rotary air blowing device is connected.
6. blow device according to claim 1, it is characterised in that the bottom within described purging main body case is provided with flue-dust retainer, is provided with, at the box bottom purging main body case, the ash hole being connected with described flue-dust retainer.
7. blow device according to claim 6, it is characterised in that described inactivation SCR denitration catalyst is placed in described flue-dust retainer top by net-shaped steel structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521052416.4U CN205269412U (en) | 2015-09-11 | 2015-12-16 | Inactivation SCR denitration catalyst sweep device |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2015105774408 | 2015-09-11 | ||
| CN201510577440 | 2015-09-11 | ||
| CN201521052416.4U CN205269412U (en) | 2015-09-11 | 2015-12-16 | Inactivation SCR denitration catalyst sweep device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205269412U true CN205269412U (en) | 2016-06-01 |
Family
ID=55366414
Family Applications (5)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521052278.XU Expired - Fee Related CN205269680U (en) | 2015-09-11 | 2015-12-16 | Airtight belt cleaning device and regeneration system of inactivation SCR denitration catalyst |
| CN201521052416.4U Expired - Fee Related CN205269412U (en) | 2015-09-11 | 2015-12-16 | Inactivation SCR denitration catalyst sweep device |
| CN201510943164.2A Expired - Fee Related CN105381716B (en) | 2015-09-11 | 2015-12-16 | A kind of blow device of inactivation SCR denitration catalyst, activation device and regenerative system and corresponding method |
| CN201510943466.XA Expired - Fee Related CN105363500B (en) | 2015-09-11 | 2015-12-16 | The closed cleaning device and method and regenerative system and method for a kind of inactivation SCR denitration catalyst |
| CN201521051815.9U Expired - Fee Related CN205269679U (en) | 2015-09-11 | 2015-12-16 | Activation device of inactivation SCR denitration catalyst |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521052278.XU Expired - Fee Related CN205269680U (en) | 2015-09-11 | 2015-12-16 | Airtight belt cleaning device and regeneration system of inactivation SCR denitration catalyst |
Family Applications After (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510943164.2A Expired - Fee Related CN105381716B (en) | 2015-09-11 | 2015-12-16 | A kind of blow device of inactivation SCR denitration catalyst, activation device and regenerative system and corresponding method |
| CN201510943466.XA Expired - Fee Related CN105363500B (en) | 2015-09-11 | 2015-12-16 | The closed cleaning device and method and regenerative system and method for a kind of inactivation SCR denitration catalyst |
| CN201521051815.9U Expired - Fee Related CN205269679U (en) | 2015-09-11 | 2015-12-16 | Activation device of inactivation SCR denitration catalyst |
Country Status (1)
| Country | Link |
|---|---|
| CN (5) | CN205269680U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105381716A (en) * | 2015-09-11 | 2016-03-09 | 福建紫荆环境工程技术有限公司 | Deactivated SCR denitration catalyst purging device, activation device and regeneration system and corresponding methods |
| CN105921015A (en) * | 2016-07-04 | 2016-09-07 | 青岛双瑞海洋环境工程股份有限公司 | Soot blowing system of denitrification reactor |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106017001A (en) * | 2016-07-14 | 2016-10-12 | 江苏龙净科杰催化剂再生有限公司 | Drying device special for honeycomb type selective catalytic reduction (SCR) denitration catalyst regeneration |
| CN108057462B (en) * | 2017-11-17 | 2020-06-30 | 四川大学 | Regeneration method of carbon-based non-metallic desulfurizer |
| CN107961818A (en) * | 2017-12-06 | 2018-04-27 | 南京威安新材料科技有限公司 | The renovation process and production equipment of flue gas SCR catalyst |
| CN109046023B (en) * | 2018-07-12 | 2020-12-22 | 哈尔滨工程大学 | SCR reactor soot blowing system and method |
| CN109833733B (en) * | 2019-03-06 | 2021-10-15 | 深圳市傲月光电科技有限公司 | Cleaning device for low temperature plasma exhaust-gas treatment |
| CN111960429B (en) * | 2020-08-26 | 2022-07-12 | 万华化学集团股份有限公司 | Preparation method of hierarchical porous aluminum phosphate molecular sieve catalyst, catalyst prepared by hierarchical porous aluminum phosphate molecular sieve catalyst and application of hierarchical porous aluminum phosphate molecular sieve catalyst in olefin isomerization |
| CN113019471B (en) * | 2021-02-07 | 2023-05-23 | 铜仁市诚一环保科技有限公司 | Method and equipment for cleaning denitration catalyst |
| CN113769583B (en) * | 2021-10-08 | 2024-01-26 | 安徽元琛环保科技股份有限公司 | Regeneration method of baking-free dust removal denitration ceramic filter tube |
| CN114367196A (en) * | 2021-12-01 | 2022-04-19 | 苏州西热节能环保技术有限公司 | Method for regenerating SCR denitration catalyst by online semidry method |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1157410A (en) * | 1997-08-19 | 1999-03-02 | Babcock Hitachi Kk | Device and method for regenerating alkali-deteriorated denitrification catalyst |
| US6929701B1 (en) * | 2003-06-03 | 2005-08-16 | Scr-Tech Llc | Process for decoating a washcoat catalyst substrate |
| US8048818B2 (en) * | 2008-03-26 | 2011-11-01 | Babcock & Wilcox Power Generation Group, Inc. | In-situ regeneration of a catalyst masked by calcium sulfate |
| CN201445960U (en) * | 2009-04-29 | 2010-05-05 | 常州市肯创环境工程技术有限公司 | Structure of catalyst cleaning and regenerating device |
| CN102658170B (en) * | 2012-04-11 | 2014-09-03 | 西安交通大学 | Regeneration technology of V-Ti-based honeycomb SCR denitration catalyst, and apparatus thereof |
| CN103071545A (en) * | 2012-12-25 | 2013-05-01 | 北京国电龙源环保工程有限公司 | Ultrasonic cleaning device and method for regenerating catalyst |
| CN203508041U (en) * | 2013-09-17 | 2014-04-02 | 北京北科欧远科技有限公司 | Flue gas denitrification catalyst cleaning-regeneration device |
| CN203971958U (en) * | 2014-04-11 | 2014-12-03 | 武汉梅斯特工程技术有限公司 | A kind of SCR catalyst regeneration device |
| CN205269680U (en) * | 2015-09-11 | 2016-06-01 | 福建紫荆环境工程技术有限公司 | Airtight belt cleaning device and regeneration system of inactivation SCR denitration catalyst |
-
2015
- 2015-12-16 CN CN201521052278.XU patent/CN205269680U/en not_active Expired - Fee Related
- 2015-12-16 CN CN201521052416.4U patent/CN205269412U/en not_active Expired - Fee Related
- 2015-12-16 CN CN201510943164.2A patent/CN105381716B/en not_active Expired - Fee Related
- 2015-12-16 CN CN201510943466.XA patent/CN105363500B/en not_active Expired - Fee Related
- 2015-12-16 CN CN201521051815.9U patent/CN205269679U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105381716A (en) * | 2015-09-11 | 2016-03-09 | 福建紫荆环境工程技术有限公司 | Deactivated SCR denitration catalyst purging device, activation device and regeneration system and corresponding methods |
| CN105381716B (en) * | 2015-09-11 | 2018-03-20 | 福建紫荆环境工程技术有限公司 | A kind of blow device of inactivation SCR denitration catalyst, activation device and regenerative system and corresponding method |
| CN105921015A (en) * | 2016-07-04 | 2016-09-07 | 青岛双瑞海洋环境工程股份有限公司 | Soot blowing system of denitrification reactor |
| CN105921015B (en) * | 2016-07-04 | 2019-08-09 | 青岛双瑞海洋环境工程股份有限公司 | The soot blower system of Benitration reactor |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105381716A (en) | 2016-03-09 |
| CN105381716B (en) | 2018-03-20 |
| CN105363500B (en) | 2018-06-19 |
| CN205269680U (en) | 2016-06-01 |
| CN105363500A (en) | 2016-03-02 |
| CN205269679U (en) | 2016-06-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205269412U (en) | Inactivation SCR denitration catalyst sweep device | |
| CN109260845B (en) | A kind of environment-friendly type industrial waste-gas purifier and exhaust gas purifying method | |
| CN103055962B (en) | Selective catalystic reduction (SCR) denitration catalyst reactivation method | |
| CN210448525U (en) | Waste gas treatment environmental protection equipment | |
| CN206273325U (en) | A kind of dust filter unit | |
| CN208193968U (en) | A kind of environment protection kitchen treating apparatus for exhaust gas of oil smoke | |
| CN104707462B (en) | A kind of waste gas produced in time preparing fertilizer removes ammonia and the method for dust | |
| CN210045076U (en) | Waste gas purification device for environmental protection | |
| CN210021611U (en) | Waste gas treatment device in injection molding process | |
| CN203663649U (en) | Dust removal device for tailored blank laser welding | |
| CN103691248B (en) | A kind of laser assembly solder dust arrester | |
| CN203648552U (en) | SCR (Semiconductor Control Rectifier) catalyst regeneration device | |
| CN105944547A (en) | Absorption tower device with ultralow emission of flue gas and application | |
| CN212999050U (en) | Spray treatment device of vertical waste gas washing tower | |
| CN110624342A (en) | Filter equipment of paint spray booth waste gas | |
| CN109316875A (en) | A kind of technique and spraying box handling coating cloud | |
| CN109751647B (en) | Automatic wash electrostatic precipitator unit's lampblack absorber | |
| CN220824656U (en) | Flue gas denitration equipment | |
| CN214812020U (en) | Novel paint spray booth abandonment processing device | |
| CN214635357U (en) | Paper deacidification system with inhale fog function | |
| CN215539668U (en) | Interior decoration absorbs processing apparatus with good formaldehyde of feature of environmental protection | |
| CN216856027U (en) | Tail gas treatment device for PBAT and PBT polycondensation | |
| CN219897649U (en) | Waste gas spray tower | |
| CN217367829U (en) | Superoxide nanometer microbubble equipment for improving coating waste gas purification effect | |
| CN217615325U (en) | High coal stove electric precipitation washing unit |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160601 Termination date: 20181216 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |