CN210320063U - Carbonization incinerator for treating solid waste material - Google Patents
Carbonization incinerator for treating solid waste material Download PDFInfo
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- CN210320063U CN210320063U CN201921171105.8U CN201921171105U CN210320063U CN 210320063 U CN210320063 U CN 210320063U CN 201921171105 U CN201921171105 U CN 201921171105U CN 210320063 U CN210320063 U CN 210320063U
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Abstract
The utility model discloses a carbonization incinerator for treating solid waste materials, which is used for carbonizing and incinerating solid waste materials, and comprises a primary combustion system, a secondary combustion system and a discharge system which are connected in sequence, wherein the primary combustion system is in an inclined design and is provided with a pulse rotary turning plate unit, a primary combustion chamber and a combustion mechanism, the pulse rotary turning plate unit is arranged in the primary combustion chamber, the combustion mechanism is arranged at the bottom of the primary combustion chamber, the solid waste materials to be incinerated are overturned and conveyed through the pulse rotary turning plate unit to complete the drying process, and are combusted in the primary combustion chamber, harmful smoke generated by combustion enters the secondary combustion system, and a secondary gas combustion chamber is arranged in the secondary combustion system and is used for carrying out high-temperature incineration on the harmful smoke generated by the solid waste materials; the discharging system comprises a slag discharging mechanism and a smoke discharging mechanism, wherein the slag discharging mechanism is arranged at the bottom of the primary combustion chamber, and a dust removing system is arranged in the smoke discharging mechanism and used for discharging dust removed gas generated by incineration.
Description
Technical Field
The utility model relates to a waste treatment's technical field, more specifically relates to a handle carbomorphism of solid waste material and burn burning furnace.
Background
In the process of urbanization, garbage is once a burden for urban development as a product of urban metabolism, and many cities in the world have the situation of surrounding garbage. The waste incineration method is a waste treatment method practiced for many years. Compared with the landfill method, the method has the advantages of small floor area and high efficiency, and once the method is regarded as a good method of 'reducing weight quickly', and attracts the strong development of developed countries such as Japan, Germany and the like.
The waste incineration is a process of subjecting waste to oxidation at a high temperature by appropriate thermal decomposition, combustion, melting, or other reaction to reduce the volume of the waste to form a residue or a molten solid substance. However, the existing garbage incinerators are large, occupy a large area, have high investment cost, and have low incineration disposal rate during the incineration process of garbage and waste, so that a large amount of waste gas, heat and powder layer are generated, and if the incinerated waste gas is not properly treated, the problems of secondary pollution and the like are easily caused, and the problem of environmental deterioration is also endless.
SUMMERY OF THE UTILITY MODEL
For overcoming current technical defect, the utility model provides a handle carbomorphism of solid waste material and burn burning furnace has simple structure, burns the beneficial effect that the processing rate is high, emission control level is high.
For realizing the purpose of the utility model, the following technical scheme is adopted to realize:
a carbonization incinerator for treating solid waste materials is used for carbonizing and incinerating the solid waste materials and comprises a primary combustion system, a secondary combustion system and a discharge system which are sequentially connected, wherein the primary combustion system is in an inclined design and is provided with a pulse rotary turning plate unit, a primary combustion chamber and a combustion mechanism, the pulse rotary turning plate unit is arranged in the primary combustion chamber, the combustion mechanism is arranged at the bottom of the primary combustion chamber, the combustion mechanism comprises but is not limited to a combustor, a burner or a biomass particle burner, the solid waste materials to be incinerated are in the primary combustion chamber and are overturned and conveyed through the pulse rotary turning plate unit to complete a drying process, and carbonization and incineration are carried out, and a secondary gas combustion chamber is arranged in the secondary combustion system and is used for carrying out high-temperature incineration on harmful smoke generated after the solid waste materials are combusted; the discharging system comprises a slag discharging mechanism and a smoke discharging mechanism, wherein the slag discharging mechanism is arranged at the bottom of the primary combustion chamber, and a dust removing system is arranged in the smoke discharging mechanism and used for discharging dust removed gas generated by incineration.
The technical scheme is mainly used for carbonizing and incinerating solid materials and can also be used for treating other waste materials. Wherein, this technical scheme's a combustion system is the tilting design, and broken solid waste material turns over the board unit through the pulsation gyration and turns over and downward overturn the conveying step by step, accomplishes drying process, and reliable, durable.
In this technical scheme, adopt the gas combustion machine to carry out the degree of depth burning to the high temperature flue gas that solid waste material produced in the secondary gas combustion chamber, the gas combustion machine can heat the high temperature flue gas and heat up to more than 1000 ℃ to keep burning more than 2 seconds, the rethread goes out the dust pelletizing system of cigarette mechanism and removes dust the back and discharges.
The smoke discharging mechanism is internally provided with a dust removing system, and the smoke is subjected to harmless treatment through the dust removing effect of the dust removing system, so that the pollution of the discharged smoke to the atmospheric environment is avoided.
The slag discharging mechanism is designed in a groove type, can effectively discharge ash, and can prevent heat from being dissipated and overflowing. The slag discharging mechanism is provided with a groove type roller slag discharging port, and anti-overflow heat protection plates are arranged on two sides of the groove type roller slag discharging port.
Further, a combustion mechanism is arranged at the bottom of the primary combustion chamber, and the combustion mechanism comprises but is not limited to a combustor, a combustor or a biomass particle combustor. Used for heating, carbonizing and incinerating solid waste materials and improving the temperature of the primary combustion chamber.
A burner or a burner in the combustion mechanism is adopted in the primary combustion chamber for combustion heating, so that the temperature in the furnace can be effectively increased, and the temperature is increased to 500-700 ℃. Under the heating and burning action of the burner or the burner, high-temperature flue gas, nitric oxide, carbon monoxide and other organic waste gases in the incinerator are gathered to the top of the primary combustion system, and are introduced into the secondary gas combustion chamber by the induced draft fan to be fully combusted with high-temperature flame sprayed out from the gas combustion chamber.
Furthermore, the primary combustion system is provided with a plurality of groups of pulse rotary turning plate units, the pulse rotary turning plate units are sequentially turned and connected and are driven step by step to turn the solid waste materials step by step in the primary combustion chamber for combustion, and the pulse rotary turning plate units are arranged above the primary combustion chamber.
Furthermore, a thermal radiation material flow guide partition plate is arranged between the primary combustion system and the secondary combustion system, solid waste materials on the pulse rotary turning plate unit are in contact with the thermal radiation flow guide partition plate after being turned over, and heat generated by combustion of the secondary gas combustion chamber is conducted to the thermal radiation material flow guide partition plate, so that the temperatures of the primary combustion chamber and the solid waste materials are improved.
In the technical scheme, the material on the upper-stage pulse rotary turning plate unit is thrown onto the heat radiation flow guide partition plate to be fully contacted with the heat radiation flow guide partition plate and slides into the lower-stage pulse rotary turning plate unit. The heat radiation material diversion baffle is designed in an inclined mode and is used for conducting heat generated by the secondary gas combustion chamber into the primary combustion chamber, and then drying, carbonization and combustion of solid waste materials are accelerated. The heat generated by the combustion of the secondary gas combustion chamber is conducted to the heat radiation material diversion partition plate, and then the temperature of the material and the temperature of the primary combustion chamber are improved.
Furthermore, the primary combustion system further comprises a material conveying mechanism, a feeding hopper and a feeding mechanism, wherein the material conveying mechanism is in an inclined design and conveys solid waste materials to the feeding hopper, the feeding hopper is connected with the feeding mechanism and arranged at the top of the pulse rotary turning plate unit, the feeding mechanism is provided with a groove type roller feeding opening, anti-overflow heat protection plates are arranged on two sides of the feeding opening, and the pulse rotary turning plate unit is turned and reset to be connected with the feeding mechanism.
The feeding mechanism is designed in a groove mode, the material conveying mechanism conveys materials to the feeding hopper from bottom to top, the feeding hopper conveys the materials to the feeding mechanism, and the feeding mechanism feeds quantitative materials to the pulsating rotary turning plate unit to ensure orderly carbonization and incineration in the furnace. Anti-overflow heat protection plates are arranged on two sides of the feeding port, and are mainly used for preventing heat dissipation.
Further, go out the top switch-on of cigarette mechanism and secondary gas combustion chamber, and go out and be equipped with two sets of dust pelletizing systems who handles different grade type waste gas at least in the cigarette mechanism, dust pelletizing system connects gradually, and last a set of dust pelletizing system's rear connection has a discharge pipe, and the flue gas in the cigarette mechanism loops through dust pelletizing system dust removal processing back, discharges through the discharge pipe.
In the technical scheme, the two groups of dust removal systems are respectively a hydraulic dust removal system and a cloth bag dust removal system and are used for carrying out innocent treatment on different waste gases, and the treatment efficiency and the purification rate are higher.
Furthermore, at least 3 groups of pulse rotary turning plate units are arranged in the primary combustion system in the horizontal direction, and the 3 groups of pulse rotary turning plate units are sequentially turned and conveyed in the horizontal direction.
Furthermore, at least 3 groups of pulse rotary turning plate units are arranged in the primary combustion system in the vertical direction, the pulse rotary turning plate units in the horizontal direction and the vertical direction are sequentially transmitted in an S-shaped sequence, and after the pulse rotary turning plate units in the horizontal direction are transmitted, the pulse rotary turning plate units in the next stage and adjacent pulse rotary turning plate units continue to transmit.
In the technical scheme, the pulse rotary turning plate unit group designed in the S-shaped trend lengthens the turning and conveying distance of the solid waste, and after the solid waste is sequentially turned and conveyed in the horizontal direction, the solid waste is turned and conveyed step by step from top to bottom in a relay manner to complete the processes of drying, carbonization, incineration and ashing.
A working method of a carbonization incinerator for treating solid waste materials is suitable for the carbonization incinerator for treating the solid waste materials, and comprises the following working steps: s1: starting a primary combustion system, and heating the temperature in the incinerator to 500-700 ℃; s2: conveying the crushed solid waste material to a pulse rotary turning plate unit; s3: the pulsating rotary plate turnover unit turns over and conveys the solid waste materials, and in the turning process, high-temperature gas generated in the primary combustion chamber is fully contacted with the solid waste materials to complete the drying process; s4: the solid waste material is quickly carbonized, combusted and cracked in the primary combustion chamber until the combustible of the solid waste material is burnt into ash, and the residual residue falls into the slag discharging mechanism and is discharged by the slag discharging mechanism; s5: high-temperature flue gas generated by burning solid waste materials floats on the middle upper part of the primary combustion system, is gathered towards the top and is introduced into the secondary gas combustion chamber by the induced draft fan, high-temperature flame sprayed by the combustion of the gas in the secondary gas combustion chamber is mixed with the high-temperature flue gas and fully burns the high-temperature flue gas to form high-temperature plasma flame with the temperature of more than 1000 ℃, and the flame is kept for more than 2 seconds, so that the waste gas is fully decomposed; s6: the decomposed smoke enters a dust removal system through a smoke outlet mechanism, and is discharged after dust removal reaches the standard.
Furthermore, the primary combustion system comprises a plurality of groups of pulse rotation turning plate units, wherein the pulse rotation turning plate units are at least provided with 3 groups in the horizontal direction and sequentially turn over and convey, at least 3 stages are arranged in the vertical direction, the pulse rotation turning plate units are in S-shaped conveying, after the pulse rotation turning plate units in the same stage turn over and convey in the horizontal direction, the pulse rotation turning plate units continue to convey to the next stage and the adjacent pulse rotation turning plate units, the former pulse rotation turning plate unit turns over and conveys to the next pulse rotation turning plate unit and then resets, and the like.
Furthermore, a combustion mechanism is arranged at the bottom of the primary combustion chamber and used for combusting solid waste materials, heating the temperature in the primary combustion chamber to 500-700 ℃, and after the solid waste materials are conveyed in the primary combustion chamber step by step through a pulsating rotary plate turnover unit, rapidly carbonizing and combusting under the heating and combustion action of the combustion mechanism; the residual ash falls into a slag discharging mechanism, and high-temperature flue gas generated by combustion enters a secondary gas combustion chamber to be mixed with gas, and high-temperature combustion is continued to complete the decomposition of waste gas; and a heat radiation flow guide partition plate is arranged between the secondary gas combustion chamber and the primary combustion chamber, and the secondary gas combustion chamber transfers heat to the primary combustion chamber through the heat radiation flow guide partition plate, so that the drying of solid waste materials is accelerated, and the temperature of the primary combustion chamber is also raised.
Compared with the prior art, the technical scheme has the following beneficial effects:
(1) this technical scheme can effectively carry out the carbomorphism to solid waste material and burn to in the carbomorphism incineration process, turn over the board unit through multiunit pulsation gyration and carry out effective drying to the material, carry out rapid heating up through a combustion chamber, and quick carbomorphism combustible substance, harmful flue gas that the rethread secondary gas combustion chamber produced carries out abundant burning decomposition, and dust pelletizing system through the different grade type carries out innoxious dust removal to the flue gas at last and handles, makes the flue gas that discharges out accord with the standard.
(2) This technical scheme collects the design of chain, rotation, pulsed, mechanical type, vertical, horizontal, tilting as an organic whole to have carbonization and burn two functions, compare other incinerator and have better result of use.
(3) The technical scheme can effectively treat industrial garbage, household garbage, hospital garbage, waste rubber tires and other wastes, has wide treatment range, is particularly suitable for industrial solid wastes, and has the advantages of good treatment effect, high combustion heat efficiency and energy conservation.
(4) The technical scheme has high automation level and low operation and maintenance cost, and saves manpower and material resources.
(5) The technical scheme has high reliability and low failure rate.
(6) According to the technical scheme, the flue gas is subjected to deep combustion treatment through the gas combustion chamber, the combustion temperature is as high as 1000 ℃, and the retention time is more than 2 seconds, so that harmful components of the flue gas, such as dioxin, can be effectively decomposed, the control level of emissions is effectively improved, and the flue gas emissions meet the emission standards.
(7) This technical scheme has designed the pulsation gyration and has turned over the board unit and overturn the conveying to the material, and is not only reliable, durable, can also effectively dry the material, and the board unit has self-cleaning function, can effectively reduce clear number of times through the pulsation gyration simultaneously.
Drawings
Fig. 1 is a schematic view of the working process of the present invention.
Fig. 2 is a structure enlarged view of the pulsating rotary flap unit of the present invention.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention clearer, embodiments of the present invention are described in further detail below with reference to the accompanying drawings.
Example 1
As shown in fig. 1 and 2, a carbonization incinerator for treating solid waste materials, which is used for carbonizing and incinerating solid waste materials, comprises a primary combustion system, a secondary combustion system and a discharge system which are connected in sequence, wherein the primary combustion system is in an inclined design, 3 groups of pulse rotary plate-turning units and a primary combustion chamber 4 are arranged in the horizontal direction, the 3 groups of pulse rotary plate-turning units are respectively a first pulse rotary plate-turning unit A, a second pulse rotary plate-turning unit B and a third pulse rotary plate-turning unit C, the 3 groups of pulse rotary plate-turning units are designed step by step and turn and convey solid waste materials to be incinerated step by step in an S-shaped direction to complete a drying process, and harmful smoke generated by carbonization and incineration in the primary combustion chamber 4 enters the secondary combustion system for further deep combustion,
a secondary gas combustion chamber 7 is arranged in the secondary combustion system and is used for carrying out high-temperature incineration on harmful flue gas generated by solid waste materials; the discharge system includes slag discharging mechanism 10 and smoke discharging mechanism 11, slag discharging mechanism 10 is arranged at the bottom of primary combustion chamber 4, and a dust removing system is arranged in smoke discharging mechanism 11 and used for removing dust from gas generated by incineration and then discharging the gas.
As shown in fig. 1, the dust removal system comprises a hydraulic dust removal system 8 and a cloth bag dust removal system 9, and is used for treating different types of waste gas, so that the treatment effect is better; and the tail part of the cloth bag dust removal system 9 is provided with a discharge pipe 12 for discharging the flue gas after dust removal reaches the standard.
Wherein, adopt gas combustion engine 6 to carry out the degree of depth burning to the high temperature flue gas that solid waste material produced in the secondary gas combustion chamber 7, the gas combustion engine can heat the high temperature flue gas and rise to more than 1000 ℃ to keep burning more than 2 seconds, the rethread goes into the dust pelletizing system of cigarette mechanism 11 and removes dust and then discharges.
Wherein, the bottom of the primary combustion chamber 4 is provided with a combustion mechanism 5 for heating and combusting solid waste materials and improving the temperature of the primary combustion chamber 4. The bottom of the primary combustion chamber 4 is heated by combustion of the combustion mechanism 5, so that the temperature in the furnace can be effectively increased, and the temperature is increased to 500-700 ℃.
Wherein, be equipped with heat radiation material water conservancy diversion baffle 13 between primary combustion system and the secondary combustion system, the board unit upset is turned over in the pulsation gyration is connected with heat radiation water conservancy diversion baffle 13, the heat conduction that the burning of secondary gas combustion chamber 7 produced is to heat radiation material water conservancy diversion baffle 13 on, and then improves the temperature of primary combustion chamber.
The primary combustion system further comprises a material conveying mechanism 1, a feed hopper 2 and a feeding mechanism 3, wherein the material conveying mechanism 1 is in an inclined design and conveys solid waste materials to the feed hopper 2, the feed hopper 2 and the feeding mechanism 3 are connected and arranged at the top of the pulse rotary turning plate unit, the feeding mechanism 3 is provided with a groove type roller feeding opening 31, and anti-overflow heat protection plates 32 are arranged on two sides of the feeding opening. The pulse rotary plate turnover unit is connected with the feeding mechanism 3.
The bottom of the pulse rotary turning plate unit is provided with a groove type roller slag discharge port 33, two sides of the groove type roller slag discharge port 33 are also provided with anti-overflow heat protection plates 32, and the slag discharge port 33 is connected with the slag discharging mechanism 10.
Wherein, feed mechanism 3 is the design of recess formula, material transport mechanism 1 conveys feeder hopper 2 with the material input from the bottom up, and feeder hopper 2 conveys the material to feed mechanism 3, and feed mechanism 3 gives the board unit is turned over in the pulsation gyration with quantitative material feed, guarantees to carry out the carbomorphism in the stove in order and burns.
A working method of a carbonization incinerator for treating solid waste materials is suitable for the carbonization incinerator for treating the solid waste materials, and comprises the following working steps:
s1: starting a primary combustion system, and heating the temperature in the incinerator to 500-700 ℃;
s2: conveying the crushed solid waste materials to a feeding mechanism 3 of a feeding port 2 through a conveying mechanism 1, and feeding the materials to a pulsating rotary turning plate unit by the feeding mechanism 3 in an equivalent amount;
s3: the first pulse rotary turning plate unit A turns over and conveys solid waste materials, the materials are conveyed to the second pulse rotary turning plate conveying unit B, the first pulse rotary turning plate unit A resets, the second pulse rotary turning plate unit B turns over and conveys the materials to the third pulse rotary turning plate unit C, the second pulse rotary turning plate unit B resets, the third pulse rotary turning plate unit C conveys the materials to the heat radiation material guide plate 13, then the materials fall into the next stage and the adjacent pulse rotary turning plate unit from the heat radiation material guide plate 13, and so on, in the turning process, high-temperature smoke generated by the primary combustion chamber is fully contacted with the solid waste materials, and the drying process is completed;
s4: the solid waste material is rapidly carbonized, combusted and cracked in the primary combustion chamber 4 until the combustible of the solid waste material is burnt into ash, and the residual residue falls into the slag discharging mechanism and is discharged by the slag discharging mechanism 10;
s5: high-temperature flue gas generated by combustion of solid waste materials in the primary combustion chamber 4 enters a secondary gas combustion chamber 7 under the action of a fan, the high-temperature flue gas generated by the solid waste materials is deeply combusted by a gas combustor 6 in the secondary gas combustion chamber 7, high-temperature flame sprayed by combustion of the gas in the secondary gas combustion chamber 7 is mixed with the high-temperature flue gas and fully combusted to form high-temperature plasma flame above 1000 ℃, and the flame is kept for more than 2 seconds, so that the waste gas is fully decomposed;
s6: the decomposed flue gas is introduced into a hydraulic dust removal system 8 and a cloth bag dust removal system 9 of the flue gas outlet mechanism by an induced draft fan, and is discharged after dust removal reaches the standard.
The combustion mechanism 5 is used for combusting and heating solid waste materials, the combustion mechanism 5 is arranged at the bottom of the primary combustion chamber 4, the combustion mechanism comprises but is not limited to a combustor, a burner or a biomass particle burner, the temperature in the primary combustion chamber is heated to 500-700 ℃ through the heating of the combustion mechanism 5, the solid waste materials are conveyed step by step in the primary combustion chamber 4 through the pulsating rotary turning plate unit, and then are rapidly carbonized and combusted under the heating and combustion effects of the combustion mechanism 5; the residual ash falls into the slag discharging mechanism 10, and the high-temperature flue gas generated by combustion enters the secondary gas combustion chamber 7 to be mixed with the gas, and then high-temperature combustion is carried out continuously, so that the decomposition of the waste gas is completed.
Wherein, be equipped with heat radiation water conservancy diversion baffle 13 between secondary gas combustion chamber 7 and the primary combustion chamber 4, secondary gas combustion chamber 7 passes through heat radiation water conservancy diversion baffle 13 and gives the heat transfer of primary combustion chamber 4 for the drying of solid waste material, also gives the primary combustion chamber intensification simultaneously.
It is obvious that the above embodiments of the present invention are only examples for clearly illustrating the technical solutions of the present invention, and are not limitations to the specific embodiments of the present invention. Any modification, equivalent replacement, and improvement made within the spirit and principle of the present invention shall be included in the protection scope of the present invention.
Claims (7)
1. A carbonization incinerator for treating solid waste materials is used for carbonizing and incinerating the solid waste materials and is characterized by comprising a primary combustion system, a secondary combustion system and a discharge system which are sequentially connected, wherein the primary combustion system is in an inclined design and is provided with a pulse rotary turning plate unit, a primary combustion chamber and a combustion mechanism, the pulse rotary turning plate unit is arranged in the primary combustion chamber, the combustion mechanism is arranged at the bottom of the primary combustion chamber, the combustion mechanism comprises but is not limited to a combustor, a burner or a biomass particle burner, the solid waste materials to be incinerated are overturned and conveyed through the pulse rotary turning plate unit to complete a drying process, and high-temperature incineration is carried out in the primary combustion chamber, and a secondary gas combustion chamber is arranged in the secondary combustion system and is used for carrying out high-temperature incineration on harmful smoke generated by combustion of the solid waste materials; the discharging system comprises a slag discharging mechanism and a smoke discharging mechanism, wherein the slag discharging mechanism is arranged at the bottom of the primary combustion chamber, and a dust removing system is arranged in the smoke discharging mechanism and used for discharging dust removed gas generated by incineration.
2. A carbonization incinerator for treating solid waste materials as claimed in claim 1 wherein said primary combustion system is provided with a plurality of sets of pulsating rotary flap units, and said sets of pulsating rotary flap units are sequentially turned and engaged and are driven step by step for turning the solid waste materials step by step and for burning and transferring them in the primary combustion chamber, said pulsating rotary flap units being disposed above the primary combustion chamber.
3. A carbonization incinerator for treating solid waste material as claimed in claim 1 wherein a thermal radiation material guiding partition is provided between said primary and secondary combustion systems, solid waste material on the pulsating rotary flap unit is turned over and then contacted with the thermal radiation material guiding partition, and heat generated by combustion in said secondary gas combustion chamber is conducted to the thermal radiation material guiding partition, thereby increasing the temperature of the primary combustion chamber and the solid waste material.
4. A carbonization incinerator for treating solid waste material as claimed in claim 1 wherein said primary combustion system further comprises a material conveyor, a hopper and a feeder, said material conveyor is of inclined design and conveys the solid waste material to the hopper, said hopper is connected to said feeder and is located on the top of the pulsating rotary turning plate unit, said feeder is provided with a grooved drum feed port, and anti-overflow heat protection plates are located on both sides of the feeder, and the pulsating rotary turning plate unit is turned over and reset to engage with the feeder.
5. A carbonization incinerator for treating solid waste materials according to claim 1 wherein said flue gas outlet means is connected to the top of the secondary combustion system, and at least two sets of dedusting systems for treating different types of flue gas are provided in the flue gas outlet means, said dedusting systems being connected in series, and the end of the last set of dedusting system being connected to a discharge pipe, and the flue gas in the flue gas outlet means being discharged through the discharge pipe after being dedusted by the dedusting systems in series.
6. A carbonization incinerator for treating solid waste material as claimed in claim 2 wherein said primary combustion system is horizontally provided with at least 3 sets of pulsating rotary flap units, said 3 sets of pulsating rotary flap units being sequentially turned over and conveyed from the horizontal.
7. A carbonization incinerator for treating solid waste materials as claimed in claim 6 wherein said primary combustion system is provided with at least 3 sets of pulsating rotary flap units in vertical direction, the horizontal and vertical pulsating rotary flap units are sequentially transferred in S-shape sequence, and after the transfer of the horizontal pulsating rotary flap unit is completed, the next stage and the adjacent pulsating rotary flap unit are transferred continuously.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN110296416A (en) * | 2019-07-24 | 2019-10-01 | 许建军 | A kind of charing incinerator and its working method handling solid waste material |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110296416A (en) * | 2019-07-24 | 2019-10-01 | 许建军 | A kind of charing incinerator and its working method handling solid waste material |
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