CN209782667U - Incineration system based on five-chamber RTO - Google Patents
Incineration system based on five-chamber RTO Download PDFInfo
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- CN209782667U CN209782667U CN201920430416.5U CN201920430416U CN209782667U CN 209782667 U CN209782667 U CN 209782667U CN 201920430416 U CN201920430416 U CN 201920430416U CN 209782667 U CN209782667 U CN 209782667U
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Abstract
The utility model discloses an incineration system based on five room RTO, this utility model adopts five room RTO, energy utilization and energy saving aspect are better than three room RTO incineration system effect, because 3 exhaust fans are respectively installed in the RTO import and export, total throughput can reach 3 x 25000m3/h, in addition each way cooperation between the valve, the ability of handling waste gas promotes greatly, can simultaneous processing drying chamber exhaust waste gas and water dart exhaust waste gas, the effluent water sump also can connect pipeline to spray tower fan all the way.
Description
Technical Field
The utility model relates to a five room RTO waste gas burn technical field specifically are a system of burning based on five room RTO.
Background
RTO is a high-efficiency organic waste gas treatment device. Compared with the traditional catalytic combustion and direct combustion type thermal oxidation furnace, the high-efficiency direct-fired thermal oxidation furnace has the characteristics of high thermal efficiency, low operation cost, capability of treating low-concentration waste gas with large air volume and the like, and can also carry out secondary waste heat recovery when the concentration is slightly high, thereby greatly reducing the production and operation cost.
RTO, regenerative oxidation furnace, its principle is to oxidize the organic matter in the waste gas into corresponding carbon dioxide and water under high temperature to purify waste gas, and retrieve the heat that releases when waste gas decomposes, RTO major structure comprises combustion chamber, regenerator and diverter valve etc.. According to the actual requirements of customers, different heat energy recovery modes and switching valve modes are selected.
The regenerative combustion technology is a technology of combustion under the condition of high-temperature low-oxygen air, also called as high-temperature air combustion technology, also called as HTAC technology, also called as flameless combustion technology, fundamentally improves the energy utilization rate of the heating furnace, especially reasonably utilizes low-heat value fuel, reduces the emission of pollutants, saves energy, becomes an advanced technology meeting the current resource and environmental requirements, and in addition, the regenerative combustion technology also strengthens the furnace gas circulation in the heating furnace, evens the temperature field of the furnace, improves the heating quality and has very obvious effect.
The conventional incineration system is generally based on a three-chamber RTO, and due to the limitation of three chambers, the energy utilization rate and the energy saving aspect also increase the space, so an improved technology is urgently needed to solve the problem existing in the prior art.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide an incineration system based on five room RTO to solve the problem that proposes in the above-mentioned background art.
In order to achieve the above object, the utility model provides a following technical scheme: a burning system based on a five-chamber RTO comprises a drying chamber waste gas pipeline, a water spray net filtering device, a spray tower fan, a secondary spray tower, a tap water inlet, a multi-pipe net pressure explosion suppression device, a buffer tank, a water ejector waste gas pipeline, a 2# air inlet root valve, a 1# fresh air valve, a 3# fan inlet valve, a 4# fan inlet valve, a 5# fan inlet valve, an exhaust fan A, a 6# fan outlet valve, a 7# fan outlet valve, an 8# fan outlet valve, a 9# air inlet root valve, a 10# bypass valve, a five-chamber RTO, a 38# nitrogen valve, a 28# ultrahigh temperature self-control valve, a waste heat utilization boiler, a 30# high temperature discharge valve, a 31# boiler root valve, a 29# RTO air inlet switching valve, a heat exchanger, a bin to be discharged, a 32# exhaust fan inlet valve, a 33# exhaust fan inlet valve, a 34# exhaust fan inlet valve, an exhaust fan B, a 35# exhaust fan outlet valve, a 36# exhaust fan outlet valve, a 37# exhaust fan outlet valve, the waste gas pipeline of the drying chamber is connected with a water spray net filtering device, one side of the water spray net filtering device is connected with one end of a spray tower fan, the other end of the spray tower fan is connected with one end of a secondary spray tower, a tap water inlet is respectively connected with the water spray net filtering device and the secondary spray tower, the other end of the secondary spray tower is connected with one end of a multi-pipe net pressure explosion-proof device, the other end of the multi-pipe net pressure explosion-proof device is connected with one end of a buffer tank, the waste gas pipeline of a water ejector is respectively connected with the multi-pipe net pressure explosion-proof device and the spray tower fan, the other end of the buffer tank is connected with one end of a No. 2 air inlet root valve through a flame arrester, the other end of the No. 2 air inlet root valve is respectively connected with a No. 1 fresh air valve, a No. 3 fan inlet valve, a No. 4 fan inlet valve and a No. 5 fan inlet, the other sides of the three exhaust fans A are respectively provided with a 6# fan outlet valve, a 7# fan outlet valve and a 8# fan outlet valve, one ends of the 6# fan outlet valve, the 7# fan outlet valve and the 8# fan outlet valve, which are far away from the exhaust fan A, are respectively connected with a 9# air inlet root valve and one end of a 10# bypass valve, the other end of the 10# bypass valve is connected with a five-chamber RTO through a first tee joint, a 38# nitrogen valve is connected on the remaining port of the first tee joint, the top end of the five-chamber RTO is connected with one end of a 28# ultra-high temperature self-control dump valve, the other end of the 28# ultra-high temperature self-control dump valve is connected with a second tee joint, one end of the waste heat utilization boiler is connected with a second tee joint through a 30# high temperature discharge valve, the other end of the waste heat utilization boiler is connected with a third tee joint through a 31# boiler root valve, one end of the 29# RTO air inlet, one end of the heat exchanger is connected to a residual port of the third tee joint, the five-chamber RTO is far away from and connected with one end of a 10# bypass valve and the heat exchanger is far away from one end of the third tee joint and is connected with one side of a three exhaust fan B, the exhaust fan B is three, the other side of the exhaust fan B is connected with an exhaust cylinder through a 35# exhaust fan outlet valve, a 36# exhaust fan outlet valve and a 37# exhaust fan outlet valve, and the 9# air inlet root valve is far away from one end of the exhaust fan A and is connected with the exhaust cylinder.
preferably, the five-chamber RTO is provided with five chambers therein, the five-chamber RTO is provided with a # 11 RTO inlet switching valve, a # 12 RTO inlet switching valve, a # 13 RTO inlet switching valve, a # 14 RTO inlet switching valve, a # 15 RTO inlet switching valve, a # 16 RTO outlet switching valve, a # 17 RTO outlet switching valve, a # 18 RTO outlet switching valve, a # 19 RTO outlet switching valve, a # 20 RTO outlet switching valve, a # 21 RTO cold air purging valve, a # 22 RTO cold air purging valve, a # 23 RTO cold air purging valve, a # 24 RTO cold air purging valve, a # 25 RTO cold air purging valve, the # 11 RTO inlet switching valve, the # 16 RTO outlet switching valve, and the # 21 RTO cold air purging valve are located in the same chamber, the # 12 RTO inlet switching valve, the # 17 RTO outlet switching valve, and the # 22 RTO cold air purging valve are located in the same chamber, the # 13 RTO inlet switching valve, the # 18 RTO outlet switching valve, the # 23 RTO purging valve are located in the same, the air inlet switching valve of the 14# RTO, the air outlet switching valve of the 19# RTO and the cold air blowing valve of the 24# RTO are positioned in the same cavity, the air inlet switching valve of the 15# RTO, the air outlet switching valve of the 20# RTO and the cold air blowing valve of the 25# RTO are positioned in the same cavity, the cold air blowing valve of the 21# RTO, the cold air blowing valve of the 22# RTO, the cold air blowing valve of the 23# RTO, the cold air blowing valve of the 24# RTO and the cold air blowing valve of the 25# RTO are also connected with the air cooler switching valve of the 26# air cooler and the air cooler switching valve of the 27# air cooler, one side of the RTO of the five chambers is provided with an inlet valve, the other end of the RTO of the five chambers is provided with an outlet valve, the inlet valve is connected with the RTO air inlet switching valve of the 11# RTO, the RTO air inlet switching valve of the 12# RTO, the RTO air inlet switching, 19# RTO air-out diverter valve, 20# RTO air-out diverter valve link to each other, five room RTO upper surface mounting have four combustors, two at mutual interval the combustor links to each other with a combustion air fan, and two remaining combustors link to each other with a remaining combustion air fan.
Preferably, the exhaust gas line of the drying chamber has an exhaust gas discharge of at least 8000m3/h。
Preferably, the exhaust volume of each exhaust fan A and each exhaust fan B is 25000m3/h。
Preferably, a plurality of flame arresters are arranged between the waste gas pipeline of the water ejector and the multi-pipe net pressure explosion-proof device.
Compared with the prior art, the beneficial effects of the utility model are that:
(1) Five-chamber RTO is adopted in the incineration system, so that the energy utilization rate and the energy saving effect are better than those of a three-chamber RTO incineration system.
(2) Because the RTO inlet and the RTO outlet are respectively provided with 3 exhaust fans, the total treatment capacity can reach 3 multiplied by 25000m3And h, the capacity of treating waste gas is greatly improved by matching the valves of all paths.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
In the figure: drying chamber waste gas pipeline 1, water spray net filtering device 2, spray tower fan 3, secondary spray tower 4, tap water inlet 5, multi-pipe net pressure explosion-proof device 6, buffer tank 7, water jet device waste gas pipeline 8, 2# air inlet root valve 9, 1# fresh air valve 10, 3# air inlet valve 11, 4# air inlet valve 12, 5# air inlet valve 13, exhaust fan A14, 6# air outlet valve 15, 7# air outlet valve 16, 8# air outlet valve 17, 9# air inlet root valve 18, 10# bypass valve 19, five-chamber RTO20, 38# nitrogen valve 21, 28# ultra-high temperature self-control dump valve 22, waste heat utilization boiler 23, 30# high temperature exhaust valve 24, 31# boiler root valve 25, 29# RTO air inlet switching valve 26, heat exchanger 27, to-be-discharged bin 28, 32# exhaust fan air inlet valve 29, 33# exhaust fan inlet valve 30, 34# air inlet valve 31, 30# exhaust fan B32, 35# exhaust fan outlet valve 33, 36# exhaust fan outlet valve 34, The air conditioner comprises a 37# exhaust fan outlet valve 35, an exhaust barrel 36, a 11# RTO air inlet switching valve 37, a 12# RTO air inlet switching valve 38, a 13# RTO air inlet switching valve 39, a14 # RTO air inlet switching valve 40, a 15# RTO air inlet switching valve 41, a 16# RTO air outlet switching valve 42, a 17# RTO air outlet switching valve 43, a 18# RTO air outlet switching valve 44, a 19# RTO air outlet switching valve 45, a 20# RTO air outlet switching valve 46, a 21# RTO cold air purging valve 47, a 22# RTO cold air purging valve 48, a 23# RTO cold air purging valve 49, a 24# RTO cold air purging valve 50, a 25# RTO cold air purging valve 51, a 26# cold air blower switching valve 52, a 27# cold air blower switching valve 53, an inlet valve 54, an outlet valve 55, a combustor 56 and a.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1, the present invention provides a technical solution: a burning system based on a five-chamber RTO comprises a drying chamber waste gas pipeline 1, a water spray net filtering device 2, a spray tower fan 3, a secondary spray tower 4, a tap water inlet 5, a multi-pipe net pressure explosion-proof device 6, a buffer tank 7, a water ejector waste gas pipeline 8, a 2# air inlet root valve 9, a 1# fresh air valve 10, a 3# air inlet valve 11, a 4# air inlet valve 12, a 5# air inlet valve 13, an exhaust fan A14, a 6# air outlet valve 15, a 7# air outlet valve 16, an 8# air outlet valve 17, a 9# air inlet root valve 18, a 10# bypass valve 19, a five-chamber RTO20, a 38# nitrogen valve 21, a 28# ultrahigh temperature self-control valve 22, a waste heat utilization boiler 23, a 30# high temperature discharge valve 24, a 31# boiler root valve 25, a 29# RTO air inlet switching valve 26, a heat exchanger 27, a to-be discharged bin 28, a 32# exhaust fan inlet valve 29, a 33# exhaust fan inlet valve 30, a 34# exhaust fan inlet valve 31, Exhaust fans B32, 35# exhaust fan outlet valve 33, 36# exhaust fan outlet valve 34, 37# exhaust fan outlet valve 35 and exhaust barrel 36, the drying chamber waste gas pipeline 1 is connected with the water spray net filtering device 2, the exhaust amount of the drying chamber waste gas pipeline 1 is at least 8000m3H, 2 one sides of water spray net filter equipment link to each other with 3 one ends of spray tower fan, the 3 other ends of spray tower fan link to each other with 4 one ends of second grade spray tower, running water inlet 5 links to each other with water spray net filter equipment 2 and second grade spray tower 4 respectively, the 4 other ends of second grade spray tower link to each other with 6 one end of the net pressure flame proof device of multitube, the 6 other ends of net pressure flame proof device of multitube link to each other with 7 one end of buffer tank, water dart waste gas pipeline 8 links to each other with net pressure flame proof device 6 of multitube and spray tower fan 3 respectively, be provided with a plurality of spark arresters between water dart waste gas pipeline 8 and the net pressure flame proof device 6 of multitube, the 7 other ends of buffer tank pass through the spark arrester and link to each other with 9 one endA3 # fan inlet valve 11, a 4# fan inlet valve 12 and a 5# fan inlet valve 13 are connected, the 3# fan inlet valve 11, the 4# fan inlet valve 12 and the 5# fan inlet valve 13 are respectively installed on one side of three exhaust fans A14, the other side of the three exhaust fans A14 is respectively installed with a 6# fan outlet valve 15, a 7# fan outlet valve 16 and A8 # fan outlet valve 17, the 6# fan outlet valve 15, the 7# fan outlet valve 16 and the 8# fan outlet valve 17 are respectively connected with one end of a 9# air inlet valve 18 and one end of a 10# bypass valve 19 at the ends far away from an exhaust fan A14, the other end of the 10# bypass valve 19 is connected with a five-chamber RTO20 through a first tee joint, a 38# nitrogen valve 21 is connected with the remaining port of the first tee joint, the top end of the five-chamber RTO20 is connected with one end of a 28# ultra-high-temperature self-control dump valve 22, the other end of the 28# dump valve 22 is connected with a second tee joint, one end of, the other end of the waste heat utilization boiler 23 is connected with a third tee joint through a No. 31 boiler root valve 25, one end of a No. 29 RTO air inlet switching valve 26 is connected with the remaining end of the second tee joint, the other end of the No. 29 RTO air inlet switching valve 26 is connected with the third tee joint through a No. 31 boiler root valve 25, one end of a heat exchanger 27 is connected with the remaining port of the third tee joint, one end of a five-chamber RTO20, which is far away from a No. 10 bypass valve 19, and one end of the heat exchanger 27, which is far away from the third tee joint, are connected with a cabin 28 to be exhausted, the cabin 28 to be exhausted is also connected with one sides of three exhaust fans B32 through a No. 32 exhaust fan inlet valve 29, a No. 33 exhaust fan inlet valve 30 and, the No. 36 exhaust fan outlet valve 34 and the No. 37 exhaust fan outlet valve 35 are connected with the exhaust barrel 36, the end of the No. 9 intake root valve 18, far away from the exhaust fan A14, is connected with the exhaust barrel, and the exhaust volume of each exhaust fan A14 and each exhaust fan B32 is 25000 m.3/h。
Five chambers RTO20 are provided with five chambers, five chambers RTO20 is provided with 11# RTO air inlet switching valve 37, 12# RTO air inlet switching valve 38, 13# RTO air inlet switching valve 39, 14# RTO air inlet switching valve 40, 15# RTO air inlet switching valve 41, 16# RTO air outlet switching valve 42, 17# RTO air outlet switching valve 43, 18# RTO air outlet switching valve 44, 19# RTO air outlet switching valve 45, 20# RTO air outlet switching valve 46, 21# RTO cold air purging valve 47, 22# RTO cold air purging valve 48, 23# RTO cold air purging valve 49, 24# RTO cold air purging valve 50, 25# RTO cold air purging valve 51, 11# RTO air inlet switching valve 37, 16# RTO air outlet switching valve 42 and 21# RTO cold air purging valve 47 in the same chamber, 12# RTO air inlet switching valve 38, 17# RTO air outlet switching valve 43 and 22# RTO cold air purging valve 48 in the same chamber, 13# RTO air inlet switching valve 39, 13#, The 18# RTO air-out switching valve 44 and the 23# RTO cold air blowing valve 49 are located in the same chamber, the 14# RTO air-in switching valve 40, the 19# RTO air-out switching valve 45 and the 24# RTO cold air blowing valve 50 are located in the same chamber, the 15# RTO air-in switching valve 41, the 20# RTO air-out switching valve 46 and the 25# RTO cold air blowing valve 51 are located in the same chamber, the 21# RTO cold air blowing valve 47, the 22# RTO cold air blowing valve 48, the 23# RTO cold air blowing valve 49, the 24# RTO cold air blowing valve 50 and the 25# RTO cold air blowing valve 51 are further connected with the 26# air cooler switching valve 52 and the 27# air cooler switching valve 53, an inlet valve 54 is arranged on one side of a five-chamber RTO20, an outlet valve 55 is arranged on the other end of the five-chamber RTO20, the inlet valve 54 is connected with the 11# RTO air-in switching valve 37, the 12# RTO air-in, the outlet valve 55 is connected with the 16# RTO air outlet switching valve 42, the 17# RTO air outlet switching valve 43, the 18# RTO air outlet switching valve 44, the 19# RTO air outlet switching valve 45 and the 20# RTO air outlet switching valve 46, four burners 56 are mounted on the upper surface of the five-chamber RTO20, two burners 56 which are spaced from each other are connected with one combustion fan 57, and the remaining two burners 56 are connected with the remaining one combustion fan 57.
Adopt five room RTO among the burning system, energy utilization and energy saving are better than three room RTO burning system effect in the aspect of, because RTO import and export respectively install 3 exhaust fans, and total handling capacity can reach 3 x 25000m3/h, and the cooperation between each way valve in addition, the ability of handling waste gas promotes greatly, can handle drying chamber exhaust waste gas and water ejector exhaust waste gas simultaneously, and the effluent water sump also can connect pipeline to the spray column fan all the way.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (5)
1. An incineration system based on a five-chamber RTO is characterized in that: the device comprises a drying chamber waste gas pipeline (1), a water spray net filtering device (2), a spray tower fan (3), a secondary spray tower (4), a tap water inlet (5), a multi-pipe net pressure explosion-proof device (6), a buffer tank (7), a water ejector waste gas pipeline (8), a No. 2 air inlet root valve (9), a No. 1 fresh air valve (10), a No. 3 fan inlet valve (11), a No. 4 fan inlet valve (12), a No. 5 fan inlet valve (13), an exhaust fan A (14), a No. 6 fan outlet valve (15), a No. 7 fan outlet valve (16), a No. 8 fan outlet valve (17), a No. 9 air inlet root valve (18), a No. 10 bypass valve (19), a five-chamber RTO (20), a No. 38 nitrogen valve (21), a No. 28 ultra-temperature self-control dump valve (22), a waste heat utilization boiler (23), a No. 30 high-temperature discharge valve (24), a No. 31 boiler root valve (25), a No, The device comprises a heat exchanger (27), a to-be-discharged bin (28), a No. 32 exhaust fan inlet valve (29), a No. 33 exhaust fan inlet valve (30), a No. 34 exhaust fan inlet valve (31), an exhaust fan B (32), a No. 35 exhaust fan outlet valve (33), a No. 36 exhaust fan outlet valve (34), a No. 37 exhaust fan outlet valve (35) and an exhaust cylinder (36), wherein a drying room waste gas pipeline (1) is connected with a water spray net filtering device (2), one side of the water spray net filtering device (2) is connected with one end of a spray tower fan (3), the other end of the spray tower fan (3) is connected with one end of a secondary spray tower (4), a tap water inlet (5) is respectively connected with the water spray net filtering device (2) and the secondary spray tower (4), the other end of the secondary spray tower (4) is connected with one end of a multi-pipe net-pressure explosion-proof device (6), the other end of the multi-pipe net-pressure explosion-proof device (6, water dart waste gas line (8) link to each other with multicell net pressure flame proof device (6) and spray column fan (3) respectively, the buffer tank (7) other end passes through the spark arrester and links to each other with 2# air inlet root valve (9) one end, 2# air inlet root valve (9) other end with respectively with 1# fresh air valve (10) and 3# fan inlet valve (11), 4# fan inlet valve (12), 5# fan inlet valve (13) link to each other, 3# fan inlet valve (11), 4# fan inlet valve (12), 5# fan inlet valve (13) are installed respectively on three exhaust fan A (14) one side, three exhaust fan A (14) opposite side is installed 6# fan outlet valve (15), 7# fan outlet valve (16), 8# fan outlet valve (17) respectively, 6# fan outlet valve (14) one end of keeping away from exhaust fan A (14) one end respectively with 9# fan outlet valve (18) and 10# bypass valve (19) One end is connected, the other end of the 10# bypass valve (19) is connected with a five-chamber RTO (20) through a first tee joint, the 38# nitrogen valve (21) is connected with a residual port of the first tee joint, the top end of the five-chamber RTO (20) is connected with one end of a 28# ultra-high temperature self-control dump valve (22), the other end of the 28# ultra-high temperature self-control dump valve (22) is connected with a second tee joint, one end of a waste heat utilization boiler (23) is connected with the second tee joint through a 30# high temperature discharge valve (24), the other end of the waste heat utilization boiler (23) is connected with a third tee joint through a 31# boiler root valve (25), one end of a 29# RTO air inlet switching valve (26) is connected with the residual port of the second tee joint, the other end of the 29# RTO air inlet switching valve (26) is connected with the third tee joint, one end of a heat exchanger (, five rooms RTO (20) are kept away from and are connected 10# bypass valve (19) one end and heat exchanger (27) and keep away from third tee bend one end and all link to each other with waiting to arrange storehouse (28), it still advances valve (29), 33# exhaust fan through 32# exhaust fan to advance valve (30), 34# exhaust fan advances valve (31) and links to each other with three exhaust fan B (32) one side to wait to arrange storehouse (28), it is three exhaust fan B (32) opposite side links to each other with exhaust cylinder (36) through 35# exhaust fan outlet valve (33), 36# exhaust fan outlet valve (34), 37# exhaust fan outlet valve (35) respectively, 9# air inlet root valve (18) are kept away from exhaust fan A (14) one end and are continuous with the exhaust cylinder.
2. A five-compartment RTO based incineration system according to claim 1, characterised in that: the five-chamber RTO (20) is internally provided with five chambers, the five-chamber RTO (20) is internally provided with a 11# RTO air inlet switching valve (37), a 12# RTO air inlet switching valve (38), a 13# RTO air inlet switching valve (39), a14 # RTO air inlet switching valve (40), a 15# RTO air inlet switching valve (41), a 16# RTO air outlet switching valve (42), a 17# RTO air outlet switching valve (43), a 18# RTO air outlet switching valve (44), a 19# RTO air outlet switching valve (45), a 20# RTO air outlet switching valve (46), a 21# RTO cold air purging valve (47), a 22# RTO cold air purging valve (48), a 23# RTO cold air purging valve (49), a 24# RTO cold air purging valve (50) and a 25# RTO cold air purging valve (51), and the 11# RTO air inlet switching valve (37), the 16# RTO air outlet switching valve (42) and the 21# RTO cold air purging valve (47) are, the 12# RTO air inlet switching valve (38), the 17# RTO air outlet switching valve (43) and the 22# RTO cold air blowing valve (48) are positioned in the same cavity, the 13# RTO air inlet switching valve (39), the 18# RTO air outlet switching valve (44) and the 23# RTO cold air blowing valve (49) are positioned in the same cavity, the 14# RTO air inlet switching valve (40), the 19# RTO air outlet switching valve (45) and the 24# RTO cold air blowing valve (50) are positioned in the same cavity, the 15# RTO air inlet switching valve (41), the 20# RTO air outlet switching valve (46) and the 25# RTO cold air blowing valve (51) are positioned in the same cavity, the 21# RTO cold air blowing valve (47), the 22# RTO cold air blowing valve (48), the 23# RTO cold air blowing valve (49), the 24# RTO cold air blowing valve (50) and the 25# RTO cold air blowing valve (51) are further connected with the 26# cold air cooler switching valve (52) and the 27# cold air cooler cold air blowing valve (, an inlet valve (54) is arranged on one side of the five-chamber RTO (20), an outlet valve (55) is arranged on the other end of the five-chamber RTO (20), the inlet valve (54) is connected with a No. 11 RTO air inlet switching valve (37), a No. 12 RTO air inlet switching valve (38), a No. 13 RTO air inlet switching valve (39), a No. 14 RTO air inlet switching valve (40) and a No. 15 RTO air inlet switching valve (41), the outlet valve (55) is connected with a 16# RTO air outlet switching valve (42), a 17# RTO air outlet switching valve (43), an 18# RTO air outlet switching valve (44), a 19# RTO air outlet switching valve (45) and a 20# RTO air outlet switching valve (46), the five-chamber RTO (20) is characterized in that four burners (56) are arranged on the upper surface of the five-chamber RTO, two burners (56) which are spaced from each other are connected with one combustion fan (57), and the rest two burners (56) are connected with the rest one combustion fan (57).
3. A five-compartment RTO based incineration system according to claim 1, characterised in that: the exhaust gas line (1) of the drying chamber discharges at leastIs 8000m3/h。
4. A five-compartment RTO based incineration system according to claim 1, characterised in that: the exhaust volume of each exhaust fan A (14) and each exhaust fan B (32) is 25000m3/h。
5. A five-compartment RTO based incineration system according to claim 1, characterised in that: and a plurality of flame arresters are arranged between the water ejector waste gas pipeline (8) and the multi-pipe net pressure explosion-proof device (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920430416.5U CN209782667U (en) | 2019-04-01 | 2019-04-01 | Incineration system based on five-chamber RTO |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920430416.5U CN209782667U (en) | 2019-04-01 | 2019-04-01 | Incineration system based on five-chamber RTO |
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| CN209782667U true CN209782667U (en) | 2019-12-13 |
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| CN201920430416.5U Active CN209782667U (en) | 2019-04-01 | 2019-04-01 | Incineration system based on five-chamber RTO |
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