CN108036337A - Indoor condensed combustion device - Google Patents
Indoor condensed combustion device Download PDFInfo
- Publication number
- CN108036337A CN108036337A CN201711135735.5A CN201711135735A CN108036337A CN 108036337 A CN108036337 A CN 108036337A CN 201711135735 A CN201711135735 A CN 201711135735A CN 108036337 A CN108036337 A CN 108036337A
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- Prior art keywords
- conduit
- heat exchanger
- combustion device
- heater
- condensed combustion
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Classifications
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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
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/75—Multi-step processes
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/07—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases in which combustion takes place in the presence of catalytic material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
-
- 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
- B01D53/005—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 by heat treatment
-
- 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
- B01D53/86—Catalytic processes
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Incineration Of Waste (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
The present invention relates to indoor condensed combustion device, is specifically, and can exclude the VOC and odorant of indoor generation indoors, while purifies air to indoor supply, recycles heat source to enable the indoor condensed combustion device that treatment effeciency significantly improves.Interior condensed combustion device according to the present invention, the heat exchanger of operating conduit part is formed in lower end, oxidation equipment and electric heater are formed in upper end, the condensed water occurred from heat exchanger does not interfere with oxidation equipment and electric heater, but lower part is fallen on, so as to extend the service life of oxidation equipment and electric heater.The condensed water elimination produced from heat exchanger is to lower part conduit, so that too many vapor will not be produced in operating conduit part, and then avoid the influence to catalytic portions efficiency, conduit portion is operated into multiple conduits, heater housings can be taken out in the side of heater portion from rear, from catalytic portions housing is above taken out replacement can be made to become easy and safeguard and be convenient to.
Description
Technical field
The present invention relates to indoor condensed combustion device, is specifically, can be indoors for the VOC and odorant occurred indoors
Discharge is removed, while air is purified to indoor supply, the indoor concentration combustion for recycling heat source to enable treatment effeciency to significantly improve
Burner.
Background technology
In the gases of various plant emissions such as usual garbage burning factory, boiler, petroleum chemical enterprise it is general all containing odorant,
The pernicious gases such as volatile organic compounds (VOC, Volatile Organic Compound).
The pernicious gas enters after the various respiratory apparatus of people, easily causes the various diseases such as respiratory tract obstruction,
Therefore legally provide various industry spots by discharge after this pernicious gas completely processing.
The method for removing of the pernicious gas has directly-heated type burning method, and (TO, Thermal Oxidizer, can be applied in height
Temperature oxidation, decompose all processing gas effective technology), heat accumulating type incineration method (RTO, Regenerative/
Rcuperative Thermal Oxidizer, the waste heat of exhaust gas are recycled as far as possible and in order to be preheated for sucking gas, by table
The heat-storing materials such as the wide ceramics of face area directly heat rear regenerated technology), heat accumulating type catalytic combustion method (RCO,
Regenerative Catalytic Oxidizer, oxygen is carried out to save fuel cost by being catalyzed at relatively low temperatures
The technology of change) etc..
The main regenerative burner device using by heat storage type combustion method in above-mentioned pernicious gas processing method
(Regenerative Thermal Oxidizer System), the regenerative burner device is by pernicious gas with high thermal oxide
Processing.
The intrinsic heat that existing pernicious gas processing mode is directly had using pernicious gas, and supplement a small amount of heat
Produce high temperature to burn again, so as to be reduced to clean air.
Existing regenerative burner device is once in Ebrean Registered Patent publication the 1538202nd, Korean utility model registration
Mistake disclosed in No. 0335165 grade of publication.
Presently disclosed Korean Patent Room registered patent publication the 1719540th " possesses oxidation equipment and the energy again
Utilize the indoor condensed combustion system of device " (calling in the following text " existing burner ") can handle VOC indoors.
It is existing interior condensed combustion system as shown in Figure 1, including：VOC gas collection portion 110, it is collected at normal temperatures
Escaping gas, and it is arranged on the frame front of four side shapes；
Preposition strainer 120, it is twisted at the rear portion of the VOC gas collection portion, is collected from the VOC gas collection portion
Contain eliminating particle thing in material in VOC gas；
Zeolite inspissator portion 130, it is arranged on the center of bottom 210 of the four sides shape frame 200, to adsorb volatility thing
The mode of matter will be discharged to interior after the VOC gas filtering that the preposition strainer 120 passes through by main fan, then pass through itself
Inspissator portion output line supplies air to the output line of ceramic catalytic oxidation furnaces 180, by the height of ceramic catalytic oxidation furnaces 180
After warm air is cooled to certain temperature and receives, the volatile materials of adsorption zone is desorbed and is removed, then sent using solving blower fan
To heat exchanger；
Main fan 150, it is arranged on the bottom 210 at the zeolite inspissator portion rear portion, is linked by pipeline, will be in zeolite
The gas that inspissator portion 130 removes volatile materials is discharged to interior；
Heat exchanger 160, it is received is desorbed the volatile materials of removing in the zeolite inspissator portion 130, passes through heat exchange
It is allowed to rising and is transmitted to electric heater 170, receiving high-temperature process gas from ceramic catalytic oxidation furnaces is used to exchange heat, and will be used for
196 DEG C of gas transport of heat exchanger is to processing gas floss hole；
Electric heater 170, it receives 220 DEG C of gases heating containing volatile materials from the heat exchanger 160, by heating
Gas transport is to ceramic catalytic oxidation furnaces；
Ceramic catalytic oxidation furnaces 180, it receives the volatile materials of heating from the electric heater 170, utilizes catalysis
It is allowed to aoxidize, is mixed while high temperature air is transmitted to heat exchanger 160 in a part of high temperature air by zeolite inspissator portion
Zeolite inspissator portion 130 is transmitted to after the Cryogenic air that 130 output line 134 transmits, and then makes the volatile materials of adsorption zone
It is desorbed removal；
Processing gas outlet 190, it is connected to heat exchanger 160, and is arranged on 300 top side of main part, will change
The gas for being used to exchange heat in hot device is discharged to outside.
The heat exchanger, electric heater, oxidation equipment and processing gas outlet are provided entirely in operating conduit
Portion.
Technical problem
Problem present on the existing indoor condensed combustion system for possessing oxidation equipment and energy reutilization device
(but the main part 300 of the prior art is to be named as operating conduit part in the present invention) as follows：
(1) heat exchanger is arranged on the inner upper end of operating conduit part, therefore produces condensed water or drip to electric heater or urge
Change oxidation furnaces, cause the service life of oxidation equipment and electric heater to reduce.
(2) condensed water produced from heat exchanger can not discharge, and cause inner filling water steam, therefore reduce catalysis effect
Rate.
(3) when replacing heater block or catalytic portions, it will need to entirely operate conduit part and all split, be inconvenient to tie up in operation
Shield, expense also increase.
The content of the invention
Technical solution
For problems of the prior art, the present invention provides a kind of general room condensed combustion device, its composition includes：
Main body, it forms corner box-like with the cell structure of front and back and internal circulation；Inspissator portion, it is arranged on the interior of the main body
In front of portion, front forms strainer, and is provided with the driving rotating rotary concentrator of motor, the upper end of the rotary concentrator
Front is provided with desorption portion；Conduit part is operated, it is connected to the rear in the inspissator portion, is connected with multiple conduits, heat exchanger,
Heater and catalytic portions are connected to each conduit.
The composition of the operating conduit part includes：Lower part conduit, its front is provided with inflow pipe, formed with rearward upper end
Tilt open inclination opening portion；
Heat exchanger portion, its slant setting the lower part conduit inclination opening portion upper end and connection, have multiple Guan Zuo
Cross to be formed in the right side；
Right side conduit, it is communicated in the right side in the heat exchanger portion, and upper end opens；
Left side conduit, it is communicated in the left side in the heat exchanger portion, and rear forms effuser；
Connecting conduit, it is communicated in the upper end in the heat exchanger portion, and upper end forms the horizontal open portion of horizontal open；
Upper catheter, forms spatial portion among it and is in inverted " u " shape, and then is respectively communicated with the upper of the connecting conduit
Portion and the top of right side conduit, heater are inserted into fixation by heater fixed part open to the left, and right side front is formed
Open front opening port, the lower end of right side conduit side form catalytic portions.
Beneficial effect
Interior condensed combustion device, its advantage are according to the present invention,
(1) heat exchanger for operating conduit part is formed in lower end, and oxidation equipment and electric heater are formed in upper end so that
The condensed water produced from heat exchanger does not interfere with oxidation equipment and electric heater, but drips to lower part, so as to extend
The service life of oxidation equipment and electric heater；
(2) condensed water elimination produced on heat exchangers avoids operating conduit part from being full of vapor, therefore to lower part conduit
Catalytic efficiency is not interfered with, its efficiency is become maximum；
(3) conduit portion is operated into multiple conduits, the side of heater portion is can to take out heater portion housing from rear, from
Catalytic portions housing is taken out in front, replacement is become easy and is maintained easily.
Brief description of the drawings
Fig. 1 is the concept map of existing regenerative burner device；
Fig. 2 is with the preferred of the present invention
The perspective view of the indoor condensed combustion device of the formation of embodiment；
Fig. 3 is a part of decomposition diagram of the indoor condensed combustion device formed with the preferred embodiment of the present invention；
Fig. 4 is the perspective view of the operating conduit part of the indoor condensed combustion device formed with the preferred embodiment of the present invention；
Fig. 5 is that the separation of the operating conduit part of the indoor condensed combustion device formed with the preferred embodiment of the present invention is had an X-rayed
Figure；
Fig. 6 is the side exploded perspective of the operating conduit part of the indoor condensed combustion device formed with the preferred embodiment of the present invention
Figure；
Fig. 7 is the burner of the present invention and the inlet temperature and outlet temperature change chart of existing burner；
Fig. 8 is the accumulative comparision of quantity of electricity figure of burner of the present invention and existing burner；
Fig. 9 is the pernicious gas treating capacity contrast of burner of the present invention and existing burner.
【Symbol description】
10:Housing； 20:Inspissator portion；
30:Operate conduit part； 510:Upper catheter；
511:Front opening port； 512:Spatial portion；
514:Lid； 520:Heater；
521:Heater body； 530:Catalytic portions；
531:It is catalyzed guide part； 540:Right side conduit；
550:Lower part conduit； 551:Tilt opening portion；
560:Heat exchanger portion； 562:Door；
570:Left side conduit； 572:Effuser
580:Connecting conduit； 582:Horizontal open portion.
Embodiment
The direction term such as the left and right side, top, lower part and the front that are used in description of the invention, the back side be such as Fig. 4 just
In hexahedron shown in arrow, the term for referring to the direction is used.
As shown in Fig. 2-Fig. 6, the present invention includes as common indoor inspissator, its composition：Main body 10, it is with front and back
Corner box-like is formed with the cell structure of internal circulation；Inspissator portion 20, it is arranged in front of the inside of the main body 10, front
Strainer is formed, and is provided with the driving rotating rotary concentrator of motor, is provided with front of the upper end of the rotary concentrator
Desorption portion；Conduit part 30 is operated, it is connected to the rear in the inspissator portion 20, is connected with multiple conduits, heat exchanger, heater
Each conduit is connected to catalytic portions.
Operating 30 air of conduit part is flowed into from lower end by lower part conduit 550, is moved to from heat exchanger portion 560 after
Top, and after the upper catheter 510 of having heaters 520 and catalytic portions 530 is set by top, then by heat exchanger portion 560 from
The effuser 572 of left side conduit 570 is discharged.
The composition of the operating conduit part 30 includes：Lower part conduit 550, its front, which is provided with, flows into pipe 552, is formed oriented
Rear upper end tilts open inclination opening portion 551；
Heat exchanger portion 560, its slant setting the lower part conduit 550 inclination opening portion 551 upper end and connection, have
Multiple pipes 562 or so cross to be formed；
Right side conduit 540, it is communicated in the right side in the heat exchanger portion 560, and upper end opens；
Left side conduit 570, it is communicated in the left side in the heat exchanger portion 560, and rear forms effuser 572；
Connecting conduit 580, it is communicated in the upper end in the heat exchanger portion 560, and upper end forms the horizontal open of horizontal open
Portion 582；
Upper catheter 510, forms spatial portion 512 among it and is in inverted " u " shape, and then is respectively communicated with and is led in the connection
The top of pipe 580 and the top of right side conduit 540, heater 520 are inserted into by heater fixed part 514 open to the left
Fixed, right side front forms open front opening port 511, and the lower end of right side conduit side forms catalytic portions 530.
The left side upper end of the lower part conduit 550 forms rectangular inclination opening portion 551, the inclination opening portion 551
Connected with heat exchanger portion 560.
The inflow pipe 552 formed with vertical curve, is discharged by inspissator portion 20 in the right end of the lower part conduit 550
Gas flow into it is described inflow pipe 552.
" ┐ " shape of the right side of the lower part conduit 550 formed with protrusion flows into pipe 552, in the inflow pipe 552 with
The 550 right side lower end of lower part conduit for the part that portion's conduit 550 meets separates and is attached to top.
That is setting segment difference 556, in lower part, space is formed on the bottom of conduit 550, into the flowing but regardless of gas, all
Condensed water can be collected.
The lower end of the lower part conduit 550 is moved out condensed water formed with hole 554.
The heat exchanger portion 560 is internally formed multiple pipes 562, forms left and right flowing by pipe 562, upper and lower flowing is
To the flows outside of pipe 562.
The right side in the heat exchanger portion 560 forms right side conduit 540, and left side forms left side conduit 570, the left side conduit
570 block the left side in heat exchanger portion 560, and processed gas is rearward discharged by effuser 572.
The front in the heat exchanger portion 560 forms door 561, makes the replacement in heat exchanger portion 560 become easy.
The connecting conduit 580 is integrally fixed at the top in heat exchanger portion 560, formed with upper catheter 510 is horizontal fixed
Horizontal open portion 582 firmly, and it is communicated in the left side upper end of upper catheter 510.
Spatial portion 512 is formed among the upper catheter 510 and is in inverted " u " shape, so it is upper with connecting conduit 580
Portion and 540 top of right side conduit are respectively communicated with.
The left side of the upper catheter 510 forms the heater fixed part 514 of opening, and the heater 520 is inserted into interior
Portion, heater body 521 are fixed on heater fixed part 514.
The right side lower end of the upper catheter 510 has catalytic portions 530 to be inserted into fixation by being catalyzed guide part 532, it is just
Face opening port 511 opens, and catalytic portions 530 are conveniently replaceable formed with lid 514.
Insertion is fixed respectively in the right side conduit 540 for operating conduit part 30, connecting conduit 580 and upper catheter 510
The temperature sensor of each temperature can be measured.
The effuser 572 formed below of the left side conduit 570 is discharged to by the processing gas in heat exchanger portion 560.
The suction of the discharge fan (not shown) of the overall gas flowing of attachment guiding operating conduit part 30 on the effuser 572
Entrance side.
Illustrate the operating of indoor condensed combustion device formed with the preferred embodiment of the present invention below.
The indoor condensed combustion device of the present invention is arranged in the position nearer from the position of VOC or pernicious gas generation, and
Start discharge fan.
With the startup of the discharge fan, room air is passed through by inspissator portion 20 in the state of harmful components are concentrated
Nearly gas then flows into lower part conduit 550 by flowing into pipe.
Along the gas that the lower part conduit 550 moves behind the peripheral part of the pipe 562 in heat exchanger portion 560 by connection
Conduit 580 moves to heater 520.
At this time, heater 520 applies heat, the gas temperature of catalytic portions 530 is sent after about rising 310 DEG C or so to catalysis
Portion 530.
The gas temperature for reaching the catalytic portions 530 should be the active temperature of catalytic portions 530, and VOC passes through 530 oxygen of catalytic portions
Change.
As described above, the processing gas that VOC is excluded is moved by right side conduit 540, then pass through the pipe of heat exchanger 560
562 inside movement.
Heat exchange mutually occurs when passing through the peripheral part of pipe 562 into the gas for flowing into pipe 552 at this time, makes to heater
The gas of 520 movements is preheated.
It is that conduit 570 moves to the left by the processing gas inside the pipe 562 of the heat exchanger 560, eventually through
Effuser 572 is discharged fan and is discharged to outside.
When the pressure that gas passes through in the heat exchanger portion 560 becomes larger or efficiency declines, hot device portion 560 is needed to change, at this time
Door 561 is opened, by heat exchanger portion 560 from above slide take out after it is i.e. replaceable.
The heater 520 similarly takes out the heater body being fixed on heater fixing port 514 when breaking down
521, then slide and take out replacement.
The replacement of the catalytic portions 530 is first to remove lid 514, then takes out each separated catalytic portions 530 and replaces.
When condensed water occurring on the heat exchanger 560, condensing drip to the bottom surface of lower part conduit 550, the conduit 550 in lower part
556 part of segment difference form check-valves discharging condensed water.
The indoor condensed combustion device (calling in the following text " this burner ") and existing of the present invention is checked below according to various experimental results
Change between the existing burner of similar structures in existing difference and performance.
That is (main body 300 of existing burner) the institute's lamps structure of operating conduit part 30 of this burner and existing burning
Device is entirely different, so as to obtain following remarkable result.
Test the difference of the 1) inlet temperature and outlet temperature of this burner and existing burner
After experiment condition-this burner and existing burner are installed in same place, it is for 5 points from 9 points in the morning to afternoon
Its operating is only set to be surveyed at the same time to the temperature and 530 end outlet side temperature change of catalytic portions for flowing into 530 end entrance side of catalytic portions
Determine and record.
This experimental result is illustrated in fig. 7 shown below, and the inlet temperature variable quantity according to the existing burners of Fig. 7 is minimum 230 DEG C, most
Up to 360 DEG C, and continue within every 30 minutes that this change occurs, but the change of this burner is more stable, than design temperature slightly
It is microlitre higher.
That is temperature is risen to more than design temperature when the temperature drops, heater 520 operates every time, thus it is existing
Burner is that the operating of heater 520 is extremely frequent, and power consumption is big, since catalytic portions are more sensitive to design temperature, causes VOC oxygen
Change efficiency to be decreased obviously.
In contrast, this burner temperature within the time is always maintained at stablizing, and then the power consumption of heater 520 is bright
Aobvious to reduce, the efficiency of catalytic portions 530 also maximizes.
2) the accumulative electricity of this burner and existing burner contrasts for experiment
After experiment condition-this burner and existing burner are installed in same place, make it from 9 points in the morning to afternoon 5
In the state of point operating, kilowatt-hour meter is installed at 520 end of heater respectively, measures the accumulative electricity per the period.Temperature is located at 310
℃。
This experimental result becomes as shown in figure 8, from Fig. 8 as can be seen that as predicted from Fig. 8 in temperature
The block heater of change can get into smooth, and existing burner continues on electric power and keeps internal temperature.
But this burner, as predicted from Fig. 7, internal temperature does not change substantially after temperature rise first,
Heater 520 is substantially inoperative, therefore accumulative electricity does not change again after heating time first.
3) treatment effeciency of this burner and existing burner contrasts for experiment
In the state of experiment condition-this burner and existing burner are installed in same place, make its from 9 points in the morning to
5 PM operates always, and in arrival end and port of export installation gas determinator, measures VOC or pernicious gas on a time period
Discharge degree.Temperature is set in 310 DEG C.
This experimental result is as shown in figure 9, from the point of view of Fig. 9, and the pernicious gas of inflow or the concentration of VOC are high, and this burning
Device and existing burner are handled this, but from chart, the treatment effeciency of this burner is than existing burner
Efficiency is about high by 16% or so.
That is the treatment effeciency of existing burner about 83%, but this burner about 99%, its excellent effect can
To remove almost all of pernicious gas or VOC.
As shown in the experiment 1 to 3, indoor condensed combustion device of the invention is that the structure progress to operating conduit part is great
Transformation, can remove inside due to moisture caused by condensed water, hence it is evident that reduce electric usage amount, maximize treatment effeciency.
Interior condensed combustion device, the heat exchanger for operating conduit part are formed in lower end, oxidation equipment according to the present invention
Upper end is formed in electric heater, the condensed water occurred from heat exchanger does not interfere with oxidation equipment and electric heater, and
It is to fall on lower part, so as to extend the service life of oxidation equipment and electric heater.The condensed water elimination produced from heat exchanger to
Lower part conduit so that will not produce too many vapor in operating conduit part, and then avoid the influence to catalytic portions efficiency, operating is led
Pipe portion is divided into multiple conduits, and heater housings can be taken out from rear in the side of heater portion, can be from above taking-up catalytic portions shell
Body, makes replacement become easy and safeguard and be convenient to.
Although the present invention is illustrated based on preferred embodiment, it will be understood by those of ordinary skill in the art that：
It can still modify the technical solution described in foregoing embodiments, and these are changed, and do not make appropriate technical solution
Essence depart from various embodiments of the present invention described in technical solution scope.Protection scope of the present invention should be wanted according to following rights
Scope is asked to explain, and all technical solutions in its equivalents should belong to scope of the presently claimed invention.
Claims (6)
- A kind of 1. interior condensed combustion device, it is characterised in thatAs general room condensed combustion device, its composition includes：Main body, it is formed with the cell structure of front and back and internal circulation Corner box-like；Inspissator portion, it is arranged in front of the inside of the main body, and front forms strainer, and is provided with driving electricity The rotating rotary concentrator of machine, the upper end front of the rotary concentrator are provided with desorption portion；Conduit part is operated, it is connected to institute The rear in inspissator portion is stated, is connected with multiple conduits, heat exchanger, heater and catalytic portions are connected to each conduit；The operating conduit part is that air is flowed into from lower end by lower part conduit, and top is moved to after from heat exchanger portion, and After the upper catheter that having heaters and catalytic portions are set by top, then the effuser row by heat exchanger portion from left side conduit Go out.
- A kind of 2. interior condensed combustion device, it is characterised in thatAs general room condensed combustion device, its composition includes：Main body, it is formed with the cell structure of front and back and internal circulation Corner box-like；Inspissator portion, it is arranged in front of the inside of the main body, and front forms strainer, and is provided with driving electricity The rotating rotary concentrator of machine, the upper end front of the rotary concentrator are provided with desorption portion；Conduit part is operated, it is connected to institute The rear in inspissator portion is stated, is connected with multiple conduits, heat exchanger, heater and catalytic portions are connected to each conduit；The composition of the operating conduit part includes：Lower part conduit, its front are provided with inflow pipe, are tilted formed with rearward upper end Open inclination opening portion；Heat exchanger portion, its slant setting the lower part conduit inclination opening portion upper end and connection, by multiple pipes or so horizontal stroke Wear to be formed；Right side conduit, it is communicated in the right side in the heat exchanger portion, and upper end opens；Left side conduit, it is communicated in the left side in the heat exchanger portion, and rear forms effuser；Connecting conduit, it is communicated in the upper end in the heat exchanger portion, and upper end forms the horizontal open portion of horizontal open；Upper catheter, among it formed spatial portion and be in inverted " u " shape, and then be respectively communicated with the top of the connecting conduit with The top of right side conduit, heater are inserted into fixation by heater fixed part open to the left, and right side front, which is formed, to be opened Front opening port, the lower end of right side conduit side forms catalytic portions.
- 3. interior condensed combustion device according to claim 2, it is characterised in that" ┐ " shape of the right side of the lower part conduit formed with protrusion flows into pipe, in the portion for flowing into pipe and meeting with lower part conduit Lower end separates and is attached to top on the right side of the lower part conduit divided.
- 4. interior condensed combustion device according to claim 2, it is characterised in thatThe heat exchanger portion, heater are respectively with slide construction is formed and is easily replaced.
- 5. interior condensed combustion device according to claim 2, it is characterised in thatThe front of the upper catheter forms front opening port, and blocks the front opening port formed with lid.
- 6. the indoor condensed combustion device according to Claims 2 or 3, it is characterised in thatThe lower end of the lower part conduit is formed with hole.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1020170118587A KR101837060B1 (en) | 2017-09-15 | 2017-09-15 | Indoor concentration and combustion device |
| KR10-2017-0118587 | 2017-09-15 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108036337A true CN108036337A (en) | 2018-05-15 |
| CN108036337B CN108036337B (en) | 2023-01-17 |
Family
ID=61728825
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711135735.5A Active CN108036337B (en) | 2017-09-15 | 2017-11-16 | Indoor concentration burner |
Country Status (2)
| Country | Link |
|---|---|
| KR (1) | KR101837060B1 (en) |
| CN (1) | CN108036337B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112268286A (en) * | 2020-10-19 | 2021-01-26 | 南京大学环境规划设计研究院集团股份公司 | High-efficient safe heat accumulation burning VOCs clean system |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108905617A (en) * | 2018-09-07 | 2018-11-30 | 云汇环保科技南通有限公司 | A kind of catalysis oxidation heat recovery apparatus of temperature self-regulating nodal pattern |
| KR102099599B1 (en) * | 2019-09-26 | 2020-04-14 | (주)상원기계 | INDUSTRIAL HYBRID MODULE TYPE VOCs TREATING APPARATUS |
| KR102157804B1 (en) * | 2019-12-24 | 2020-09-18 | 신정순 | Regeneration Catalytic Oxidation |
| KR102456662B1 (en) | 2020-10-12 | 2022-10-19 | (주)대양이엔아이 | Packaged air pollution purification system |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS55104634A (en) * | 1979-02-07 | 1980-08-11 | Nippon Shokubai Kagaku Kogyo Co Ltd | Improved process for exhaust gas treatment by means of catalyst combustion system |
| CN101893248A (en) * | 2009-05-21 | 2010-11-24 | 杰智环境科技股份有限公司 | Energy-saving device for volatile organic waste gas treatment system |
| CN205627520U (en) * | 2016-01-15 | 2016-10-12 | 北京蓝博新科环保科技有限公司 | Organic waste gas purifying system is adsorbed to full -automatic taking off |
| CN205760473U (en) * | 2016-05-13 | 2016-12-07 | 广州市怡森环保设备有限公司 | A kind of zeolite runner cleaning equipment for waste organic gas |
| CN106247355A (en) * | 2016-09-22 | 2016-12-21 | 北京市环境卫生设计科学研究所 | A kind of high concentration foul gas catalytic oxidation deodorizing equipment and deodorizing method thereof |
| KR101719540B1 (en) * | 2016-08-10 | 2017-04-05 | 김진수 | Indoor Concentrated and Combustion System of VOC with Catalyst Oxidation device and Energy Recycling Means |
| CN106582263A (en) * | 2015-10-19 | 2017-04-26 | 江苏中科睿赛污染控制工程有限公司 | Rotary wheel adsorption concentration and catalytic oxidation device and process |
| CN106621702A (en) * | 2017-03-23 | 2017-05-10 | 合肥工业大学 | Organic exhaust gas concentration treatment device |
| CN106731483A (en) * | 2017-03-21 | 2017-05-31 | 上海兰宝环保科技有限公司 | It is suitable for the exhaust treatment system of high humility organic exhaust gas |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101172694B1 (en) * | 2005-12-19 | 2012-08-09 | 한라공조주식회사 | A car rear air conditioning device |
| DE102008011938B3 (en) * | 2008-02-29 | 2009-09-10 | Arge Schedler - Thalhammer | Device for cleaning polluted exhaust gas |
| KR20100035465A (en) * | 2008-09-26 | 2010-04-05 | 최병학 | Air cleaning system |
| KR101783877B1 (en) * | 2016-09-30 | 2017-10-11 | (주)대양이엔아이 | Indoor concentration and combustion system of voc with electric burner and energy recycling means |
-
2017
- 2017-09-15 KR KR1020170118587A patent/KR101837060B1/en active IP Right Grant
- 2017-11-16 CN CN201711135735.5A patent/CN108036337B/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS55104634A (en) * | 1979-02-07 | 1980-08-11 | Nippon Shokubai Kagaku Kogyo Co Ltd | Improved process for exhaust gas treatment by means of catalyst combustion system |
| CN101893248A (en) * | 2009-05-21 | 2010-11-24 | 杰智环境科技股份有限公司 | Energy-saving device for volatile organic waste gas treatment system |
| CN106582263A (en) * | 2015-10-19 | 2017-04-26 | 江苏中科睿赛污染控制工程有限公司 | Rotary wheel adsorption concentration and catalytic oxidation device and process |
| CN205627520U (en) * | 2016-01-15 | 2016-10-12 | 北京蓝博新科环保科技有限公司 | Organic waste gas purifying system is adsorbed to full -automatic taking off |
| CN205760473U (en) * | 2016-05-13 | 2016-12-07 | 广州市怡森环保设备有限公司 | A kind of zeolite runner cleaning equipment for waste organic gas |
| KR101719540B1 (en) * | 2016-08-10 | 2017-04-05 | 김진수 | Indoor Concentrated and Combustion System of VOC with Catalyst Oxidation device and Energy Recycling Means |
| CN106247355A (en) * | 2016-09-22 | 2016-12-21 | 北京市环境卫生设计科学研究所 | A kind of high concentration foul gas catalytic oxidation deodorizing equipment and deodorizing method thereof |
| CN106731483A (en) * | 2017-03-21 | 2017-05-31 | 上海兰宝环保科技有限公司 | It is suitable for the exhaust treatment system of high humility organic exhaust gas |
| CN106621702A (en) * | 2017-03-23 | 2017-05-10 | 合肥工业大学 | Organic exhaust gas concentration treatment device |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112268286A (en) * | 2020-10-19 | 2021-01-26 | 南京大学环境规划设计研究院集团股份公司 | High-efficient safe heat accumulation burning VOCs clean system |
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| Publication number | Publication date |
|---|---|
| KR101837060B1 (en) | 2018-03-12 |
| CN108036337B (en) | 2023-01-17 |
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