CN204114953U - Revolution vertical-type garbage incinerator - Google Patents

Revolution vertical-type garbage incinerator Download PDF

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Publication number
CN204114953U
CN204114953U CN201420530274.7U CN201420530274U CN204114953U CN 204114953 U CN204114953 U CN 204114953U CN 201420530274 U CN201420530274 U CN 201420530274U CN 204114953 U CN204114953 U CN 204114953U
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revolution
chamber
feeding roller
combustion chamber
stage firing
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CN201420530274.7U
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Chinese (zh)
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杨学勤
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Individual
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Abstract

A kind of revolution vertical-type garbage incinerator, relate to a kind of waste treating device, comprise shell, be positioned at the combustion chamber of shell, pay-off, described combustion chamber comprises first-stage firing chamber, ring-like smoke gas pyrolysis room, secondary combustion chamber, three grades of combustion chambers, fills vermiculite refractory material between shell and combustion chamber at different levels; Pay-off comprises hopper, feeding roller, transmission system are dried in revolution, and revolution is dried feeding roller and is arranged on oven dry feeding roller supporting mechanism, and is connected with the output of transmission system; Revolution is dried in feeding roller and is provided with feeding screw plate, and this cylinder one end is connected with hopper, and the other end reaches single-stage combustion chamber interior, and has the drying hole communicated with first-stage firing chamber at the position of first-stage firing chamber.The utility model is without the need to independent rubbish pre-processing device, drying plant, secondary firing equipment, and structure is simple, and working service cost is low, and firing efficiency is high, applied widely, is the ideal equipment of waste incineration.

Description

Revolution vertical-type garbage incinerator
Technical field
The utility model relates to a kind of waste treating device, particularly a kind ofly makes it reach the revolution vertical-type garbage incinerator of emission request for the treatment of solid waste.
Background technology
Existing bulky refuse burning facility mainly contains mechanical grate incinerator, fluidized bed incinerator, pyrogenation incinerator, Rotation error etc., the shortcoming of these incinerators mainly needs independently rubbish pre-processing device, drying plant, secondary firing equipment, it manufactures, mounting process is complicated, and working service cost is high.
Summary of the invention
The technical problems to be solved in the utility model is: provide a kind of manufacture, mounting process simply, the revolution vertical-type garbage incinerator that working service cost is low.
The technical scheme solved the problems of the technologies described above is: a kind of revolution vertical-type garbage incinerator, comprise shell, be positioned at the combustion chamber of shell, pay-off, described combustion chamber comprises first-stage firing chamber, ring-like smoke gas pyrolysis room, secondary combustion chamber, three grades of combustion chambers, between shell and first-stage firing chamber, ring-like smoke gas pyrolysis room, secondary combustion chamber, three grades of combustion chambers, fill vermiculite refractory material; The mouth that enters of ring-like smoke gas pyrolysis room communicates with first-stage firing chamber, and the outlet flue of ring-like smoke gas pyrolysis room communicates with secondary combustion chamber, secondary combustion chamber and three grades of combustion chamber; Described pay-off comprises hopper, feeding roller, transmission system are dried in revolution, and described revolution is dried feeding roller and is arranged on oven dry feeding roller supporting mechanism, and is connected to drive it to turn round by transmission system with the output of transmission system; Revolution is dried in feeding roller and is provided with feeding screw plate, one end that feeding roller is dried in this revolution is connected with hopper, the other end that feeding roller is dried in revolution extend into single-stage combustion chamber interior or directly extend into single-stage combustion chamber interior through three grades of combustion chambers, secondary combustion chamber, and having the drying hole communicated with first-stage firing chamber at the position of first-stage firing chamber.
Further technical scheme of the present utility model is: described revolution is dried feeding roller and is provided with automatic stirring plate in the termination being positioned at first-stage firing chamber, is provided with the broken knife plate of material at the spiral part being positioned at hopper.
Further technical scheme more of the present utility model is: be also provided with hydrops cracking room in secondary firing indoor, this hydrops cracking room is communicated with first-stage firing chamber by hydrops cracking gas outlet.
Below hopper, be also provided with the hydrops collecting chamber for collecting rubbish hydrops, the hydrops sewage pump that this hydrops collecting chamber is collected is pumped into hydrops cracking room by hydrops entrance.
Further technical scheme of the present utility model is: described first-stage firing chamber is provided with combustion-supporting combustor.
Further technical scheme of the present utility model is: at the cleaning door place of secondary combustion chamber, three grades of combustion chambers, combustion-supporting combustor is housed, and in order to improve furnace temperature, ensures to burn effect.
Described secondary combustion chamber, three grades of combustion chambers are labyrinth type combustion chamber, and this labyrinth type combustion chamber needs can be transversely arranged according to difference, also can vertical array, can be parallel to first-stage firing chamber, also can perpendicular to first-stage firing chamber.
Further technical scheme of the present utility model is: bottom first-stage firing chamber, be provided with fire grate, and has oxygen supply air outlet, and this oxygen supply air outlet is connected with air blast by ajutage; The air inlet pipe of air blast extend into revolution dries in feeding roller, and ajutage is connected with the bottom of first-stage firing chamber.
Owing to adopting said structure, the revolution vertical-type garbage incinerator of the utility model compared with prior art, has following beneficial effect:
1. simply, working service cost is lower for manufacture, mounting process:
Due to the utility model comprise first-stage firing chamber, secondary combustion chamber, three grades of combustion chambers, ring-like smoke gas pyrolysis room, revolution dry feeding roller, feeding screw plate, hopper and transmission system, be characterized in carrying out in the process fed intake drying simultaneously, precombustion, the structure of vertical fixed grate incinerator achieves material automatic turning.Therefore, the utility model integrates the large-scale environment-protecting garbage incinerating stove that feeding is dried in first-stage firing chamber, ring-like smoke gas pyrolysis room, secondary combustion chamber, three grades of combustion chambers and revolution, without the need to independent rubbish pre-processing device, drying plant, secondary firing equipment, its structure is simple, simply, working service cost is lower for manufacture, mounting process.
2. firing efficiency is high, ratio of combustion is more complete:
Due to the utility model comprise first-stage firing chamber, ring-like smoke gas pyrolysis room, secondary combustion chamber, three grades of combustion chambers, revolution dry feeding roller, feeding screw plate, hopper and transmission system.During work, rubbish enters from hopper, and revolution oven dry feeding roller turns round under the drive of transmission system, and rubbish overturns and enters first-stage firing chamber under the effect of feeding screw plate, is lighted under the effect of combustion-supporting combustor; The part being deep into hopper due to feeding screw plate is equipped with the broken knife plate of material, and the rotation of drying feeding roller with revolution can carry out fragmentation to some larger rubbish, makes incineration firing more thorough; The heat of garbage utilization first-stage firing chamber in feeding roller, secondary combustion chamber and three grades of combustion chambers burn is dried in revolution, carries out drying and precombustion in the process of carrying out feeding; In addition, revolution is dried feeding roller and is had several drying holes at the position being deep into first-stage firing chamber and communicate with first-stage firing chamber; The automatic stirring plate that feeding roller termination is equipped with is dried in revolution simultaneously, and the rotation of drying feeding roller with revolution overturns rubbish, and these designs above have all increased substantially firing efficiency; Dry in feeding roller because the air inlet pipe of air blast is also deep into revolution by the utility model, utilize the air inducing effect of air blast, dry in feeding roller in revolution and produce certain negative pressure, the high temperature of induction first-stage firing chamber, naked light enter revolution dries in feeding roller, oven dry and pre-burning are carried out to rubbish, further improves firing efficiency.
Therefore, firing efficiency of the present utility model is higher, and ratio of combustion comparatively completely, thoroughly.
3. applied widely, be the ideal equipment of waste incineration:
The utility model may be used for the burning disposal of the various rubbish such as house refuse, medical waste, industrial refuse, and its scope of application is relatively more extensive, because its cost is low, firing efficiency is high, is the ideal equipment of waste incineration.
Below, in conjunction with the accompanying drawings and embodiments the technical characteristic of the revolution vertical-type garbage incinerator of the utility model is further described.
Accompanying drawing explanation
Fig. 1 ~ Fig. 5: the structural representation of the revolution vertical-type garbage incinerator of the utility model described in embodiment one, wherein:
Fig. 1: front view;
The top view of Fig. 2: Fig. 1,
The A-A sectional view of Fig. 3: Fig. 2,
The D-D sectional view of Fig. 4: Fig. 1,
The F-F sectional view of Fig. 5: Fig. 1;
Fig. 6 ~ Fig. 7: the structural representation of the revolution vertical-type garbage incinerator of the utility model described in embodiment two, wherein:
The B-B sectional view of Fig. 6: Fig. 7, Fig. 7: front view.
In above-mentioned accompanying drawing, each label declaration is as follows:
The combustion-supporting combustor of 1-, 2-automatic stirring plate, 3-first-stage firing chamber, the ring-like smoke gas pyrolysis room of 4-, 5-shell,
6-vermiculite refractory material, 7-hydrops cracking gas outlet, 8-hydrops cracking room, 9-tri-grades of combustion chambers, 10-outlet flue,
11-hopper, the broken knife plate of 12-material, 13-air blast air inlet pipe, 14-air blast, 15-hydrops collecting chamber,
16-dries feeding roller supporting mechanism, 17-ajutage, 18-transmission system, and feeding roller is dried in 19-revolution,
20-feeding screw plate, 21-drying hole, 22-secondary combustion chamber, 23-fire grate, 24-ash hole,
25-oxygen supply air outlet, 26-tri-combustion chamber cleaning door, 27-secondary combustion chamber cleaning door, 28-observation window, 29-hydrops entrance,
The combustion-supporting combustor of 30-secondary combustion chamber and three grades of combustion chambers.
Detailed description of the invention
Embodiment one:
It is a kind of revolution vertical-type garbage incinerator disclosed in Fig. 1 ~ Fig. 5, comprise shell 5, be positioned at the combustion chamber of shell, pay-off, described combustion chamber comprises first-stage firing chamber 3, ring-like smoke gas pyrolysis room 4, secondary combustion chamber 22, three grades of combustion chambers 9, fills vermiculite refractory material 6 at shell 5 and first-stage firing chamber 3, ring-like smoke gas pyrolysis room 4, secondary combustion chamber between 22, three grades of combustion chambers 9; First-stage firing chamber 3 can be cylindrical also can be square; Ring-like smoke gas pyrolysis room 4 is bicyclic ring structures, the mouth that enters of this ring-like smoke gas pyrolysis room 4 communicates with first-stage firing chamber 3, the outlet flue of ring-like smoke gas pyrolysis room 4 communicates with secondary combustion chamber 22, secondary combustion chamber 22 is connected with three grades of combustion chambers 9, and this secondary combustion chamber 22, three grades of combustion chambers 9 are labyrinth type combustion chamber, their vertical array and be parallel to first-stage firing chamber.
Described pay-off comprises hopper 11, feeding roller 19, transmission system 18 are dried in revolution, described revolution is dried feeding roller 18 and is arranged on oven dry feeding roller supporting mechanism 16, and is connected to drive it to turn round by transmission system 18 with the output of transmission system 18; Revolution is dried in feeding roller 19 and is provided with feeding screw plate 20, one end that feeding roller 19 is dried in this revolution is connected with hopper 11, the other end that feeding roller 19 is dried in revolution extend into first-stage firing chamber 3 inside through three grades of combustion chambers 9, secondary combustion chamber 22, and has several drying holes 21 communicated with first-stage firing chamber 3 at the position of first-stage firing chamber 3.
Described revolution is dried feeding roller 19 and is provided with automatic stirring plate 2 in the termination being positioned at first-stage firing chamber 3, is provided with the broken knife plate 12 of material at the spiral part being positioned at hopper 11.Regulate revolution to dry the rotating speed of feeding roller 19 according to the water content of rubbish, adjustable oven dry and the pre-burning section time of staying are to adapt to the rubbish of different humidity.
This incinerator is also also provided with hydrops cracking room 8 in secondary combustion chamber 22, and this hydrops cracking room 8 is communicated with first-stage firing chamber 3 by hydrops cracking gas outlet 7; Below hopper 11, be also provided with the hydrops collecting chamber 15 for collecting rubbish hydrops, the hydrops that this hydrops collecting chamber 15 is collected is pumped into hydrops cracking room 8 by sewage pump by hydrops entrance 29.
This incinerator is provided with combustion-supporting combustor 1 at first-stage firing chamber 3; Bottom first-stage firing chamber 3, be provided with fire grate 23, and have oxygen supply air outlet 25, this oxygen supply air outlet 25 is connected with air blast 14 by ajutage 17; The air inlet pipe 13 of air blast 14 extend into revolution dries in feeding roller 19, and ajutage 17 is connected with the bottom of first-stage firing chamber 3.
Utilize air blast 14 air inducing effect, dry in feeding roller 19 in revolution and produce certain negative pressure, the high temperature of induction first-stage firing chamber 3, naked light enter revolution dries in feeding roller 19, carries out ovens dry and burning in advance to rubbish.
One as the present embodiment one converts, and described ring-like smoke gas pyrolysis room 4 can also be structure more than three rings or three rings.
Operation principles:
Rubbish enters from hopper 11, and revolution oven dry feeding roller 19 turns round under the drive of transmission system 18, and rubbish overturns and enters first-stage firing chamber 3 under the effect of feeding screw plate 20, is lighted under the effect of combustion-supporting combustor 1, the part that feeding screw plate 20 is deep into hopper is equipped with the broken knife plate 12 of material, and the rotation of drying feeding roller 19 with revolution can carry out fragmentation to some larger rubbish, the heat burnt in garbage utilization first-stage firing chamber 3 in revolution oven dry feeding roller 19, secondary combustion chamber 22 and three grades of combustion chambers 9, carries out drying and precombustion, to improve firing efficiency in the process of carrying out feeding, revolution is dried feeding roller 19 and is being deep into the drying hole 21 of first-stage firing chamber 3, to improve the efficiency of oven dry and precombustion, the automatic stirring plate 2 that feeding roller 19 termination is equipped with is dried in revolution simultaneously, the rotation of drying feeding roller 19 with revolution overturns the rubbish in first-stage firing chamber 3, improves firing efficiency further, the hydrops that waste transportation produces deposits to hydrops collecting chamber 15 by the hole bottom hopper 11, hydrops cracking room 8 is pumped into by hydrops entrance 29 after furnace temperature raises, utilize the high temperature burning generation to carry out cracking, the gas that cracking produces enters first-stage firing chamber 3 by cracking gas outlet 7 and burns, air blast air inlet pipe 13 is deep into revolution dries in feeding roller 19, utilize the air inducing effect of air blast 14, dry in revolution the negative pressure that in feeding roller 19, generation is certain, the high temperature of induction first-stage firing chamber 3, naked light enter revolution dries in feeding roller 19, carries out oven dry and burn in advance rubbish, burn the flue gas produced first along P to the ring-like smoke gas pyrolysis room 4 entering first-stage firing chamber 3 top, flue gas after pyrolysis is along Q to entering secondary combustion chamber 22, a burning is entered in three grades of combustion chambers 9, the effect of secondary combustion chamber and three grades of combustion-supporting combustors 30 in combustion chamber is by the initial stage of lighting at rubbish, because the temperature of each combustion chamber is lower, in order to promote temperature, combustion-supporting, improve the burning effect at the initial stage that goes into operation, the flow direction of flue gas is P---Q---W---Z---X, finally enter the follow-up smoke processing system having a negative pressure (such as: bag-type dust removing system by outlet flue 10, electrostatic precipitation system etc.).
embodiment two:
It is another kind of revolution vertical-type garbage incinerator disclosed in Fig. 6 ~ Fig. 7, this incinerator is for burning the lower or inflammable rubbish of water content, its basic structure is with embodiment one, institute's difference is: it is inner that the other end that feeding roller 19 is dried in described revolution directly extend into first-stage firing chamber 3, can reduce manufacture use cost.

Claims (8)

1. a revolution vertical-type garbage incinerator, comprise shell (5), the combustion chamber being positioned at shell, pay-off, it is characterized in that: described combustion chamber comprises first-stage firing chamber (3), ring-like smoke gas pyrolysis room (4), secondary combustion chamber (22), three grades of combustion chambers (9), between shell (5) and first-stage firing chamber (3), ring-like smoke gas pyrolysis room (4), secondary combustion chamber (22), three grades of combustion chambers (9), fill vermiculite refractory material (6); The mouth that enters of ring-like smoke gas pyrolysis room (4) communicates with first-stage firing chamber (3), and the outlet flue of ring-like smoke gas pyrolysis room (4) communicates with secondary combustion chamber (22), and secondary combustion chamber (22) is connected with three grades of combustion chambers (9); Described pay-off comprises hopper (11), feeding roller (19), transmission system (18) are dried in revolution, described revolution is dried feeding roller (19) and is arranged in oven dry feeding roller supporting mechanism (16), and is connected with the output of transmission system (18) to drive it to turn round by transmission system (18); Revolution is dried in feeding roller (19) and is provided with feeding screw plate (20), one end that feeding roller (19) is dried in this revolution is connected with hopper (11), the other end that feeding roller (19) is dried in revolution extend into first-stage firing chamber (3) inside or directly extend into first-stage firing chamber (3) inner through three grades of combustion chambers (9), secondary combustion chamber (22), and have the drying hole (21) communicated with first-stage firing chamber (3) at the position of first-stage firing chamber (3).
2. revolution vertical-type garbage incinerator according to claim 1, it is characterized in that: described revolution is dried feeding roller (19) and is provided with automatic stirring plate (2) in the termination being positioned at first-stage firing chamber (3), at the spiral part being positioned at hopper (11), the broken knife plate (12) of material is installed.
3. revolution vertical-type garbage incinerator according to claim 1, is characterized in that: in secondary combustion chamber (22), be also provided with hydrops cracking room (8), and this hydrops cracking room (8) is communicated with first-stage firing chamber (3) by hydrops cracking gas outlet (7).
4. revolution vertical-type garbage incinerator according to claim 3, it is characterized in that: be also provided with the hydrops collecting chamber (15) for collecting rubbish hydrops in hopper (11) below, the hydrops sewage pump that this hydrops collecting chamber (15) is collected is pumped into hydrops cracking room (8) by hydrops entrance (29).
5. revolution vertical-type garbage incinerator according to claim 1, is characterized in that: described first-stage firing chamber (3) is provided with combustion-supporting combustor (1).
6. revolution vertical-type garbage incinerator according to claim 1, is characterized in that: at the cleaning door place of secondary combustion chamber (22), three grades of combustion chambers (9), combustion-supporting combustor (30) is housed.
7. revolution vertical-type garbage incinerator according to claim 1, is characterized in that: described secondary combustion chamber (22), three grades of combustion chambers (9) are labyrinth type combustion chamber.
8. the revolution vertical-type garbage incinerator according to the arbitrary claim of claim 1 to 7, it is characterized in that: in first-stage firing chamber (3) bottom, fire grate (23) is installed, and having oxygen supply air outlet (25), this oxygen supply air outlet (25) is connected with air blast (14) by ajutage (17); The air inlet pipe (13) of air blast (14) extend into revolution dries in feeding roller (19), and ajutage (17) is connected with the bottom of first-stage firing chamber (3).
CN201420530274.7U 2014-07-24 2014-09-15 Revolution vertical-type garbage incinerator Withdrawn - After Issue CN204114953U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420530274.7U CN204114953U (en) 2014-07-24 2014-09-15 Revolution vertical-type garbage incinerator

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Application Number Priority Date Filing Date Title
CN201420413867.5 2014-07-24
CN201420413867 2014-07-24
CN201420530274.7U CN204114953U (en) 2014-07-24 2014-09-15 Revolution vertical-type garbage incinerator

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104235856A (en) * 2014-07-24 2014-12-24 杨学勤 Rotary vertical garbage incinerator
CN106322402A (en) * 2015-06-30 2017-01-11 许成荫 Sludge biomass fuel combustion equipment system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104235856A (en) * 2014-07-24 2014-12-24 杨学勤 Rotary vertical garbage incinerator
CN104235856B (en) * 2014-07-24 2017-05-31 杨学勤 Revolution vertical-type garbage incinerator
CN106322402A (en) * 2015-06-30 2017-01-11 许成荫 Sludge biomass fuel combustion equipment system

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GR01 Patent grant
AV01 Patent right actively abandoned
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Granted publication date: 20150121

Effective date of abandoning: 20170531