CN103162300A - Continuous type transmission sludge burning caking furnace - Google Patents
Continuous type transmission sludge burning caking furnace Download PDFInfo
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- CN103162300A CN103162300A CN2011104196243A CN201110419624A CN103162300A CN 103162300 A CN103162300 A CN 103162300A CN 2011104196243 A CN2011104196243 A CN 2011104196243A CN 201110419624 A CN201110419624 A CN 201110419624A CN 103162300 A CN103162300 A CN 103162300A
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- guipure
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Abstract
The invention discloses a continuous type transmission sludge burning caking furnace which comprises a feeding device, a transmission wire belt, a furnace body system, a sideward discharging connecting wire belt and a wire belt naturally extending ditch. The feeding device comprises a support, a feeding machine and a feeding guide roller. The furnace body system comprises a preheating chamber, a heating chamber and a steam chamber. A preheating roller and a sideward discharging connecting wire belt driving roller are arranged inside the preheating chamber. A burner nozzle and a heatproof carrier roller are arranged inside the heat chamber. A transmission roller, a tensioning roller and a carrier roller are arranged inside the steam chamber. A driving roller and a support roller are arranged inside the wire belt naturally extending ditch. The transmission wire belt twines the feeding machine, the feeding guide roller, the preheating roller, the transmission roller and the tensioning roller and penetrates the heating chamber in the middle. The sideward discharging connecting wire belt twines the sideward discharging connecting wire belt transmission roller, the heatproof carrier roller, the driving roller and the support roller and penetrates the heating chamber and the steam chamber in the middle. High temperature smoke produced after burning is transmitted to the preheating chamber so that wet sludge is heated and then dried, waste heat is used, energy is saved and burning effect is good.
Description
Technical field
The present invention relates to depollution of environment treatment facility field, be specifically related to a kind of continuous transfer sludge incineration caking stove.
Background technology
Along with the progress of society, environmental pollution phenomenon is also day by day serious in recent years, and municipal sludge is one of topmost environmental contaminants.Therefore, the mud that municipal sewage produces after treatment is nationwide the difficult problem of environmental protection always.There are the pollutants such as a large amount of bacteriums, germ and nitrogen, sulphur, chlorine, heavy metal in mud, not only are difficult to process, have a strong impact on the normal operation of sewage treatment plant, and affect bulk environment, affect people's normal life.
Treatment of Sludge now is generally that mud is directly burned, and can produce a large amount of steam when wherein wetting sludge incineration, and heat contained in steam can be recovered utilization, yet these steam contain a large amount of pernicious gases, thereby has increased the difficulty that reclaims; In addition, for mud can fully be burnt, the normal method that adopts is after wet mud is carried out drying through sludge drying machine at present, high temperature incineration in burning tower again, mummification namely normally utilizes steam to carry out heat drying, but because the original investment of Treatment of Sludge is higher, wherein dry and burning process all needs respectively heating, high temperature, and therefore such mode also can increase cost of energy.Have high temperature from the smoke mixture itself of burning in tower out, its heat distributes naturally if this part smoke mixture is left, and is not used, and is also a kind of waste of the energy.In addition, because the contained heat difference of mud is very large, the flue-gas temperature that existing incinerator produces is very unstable, has limited the further recycling of this flue gas.Therefore, existing sludge drying and incinerating technology and equipment truly has further improved necessity.
Summary of the invention
In view of this, the object of the present invention is to provide a kind of continuous transfer sludge incineration caking stove, by being provided with preheating chamber at heating clamber one end, the high-temperature flue gas that produces after burning is outputed to preheating chamber wet mud is first carried out the pre-heating temperature elevation drying, thus can UTILIZATION OF VESIDUAL HEAT IN, energy savings and burn effective.
For achieving the above object, technical scheme of the present invention is as follows:
A kind of continuous transfer sludge incineration caking stove comprises that feeding device, transmission guipure, system of bf body, side discharging switching guipure and guipure extend trench naturally;
Described feeding device comprises support, feeder and material loading deflector roll; Described system of bf body comprises preheating chamber, heating clamber and water steam chamber; Described preheating chamber top is provided with floss hole, and top is provided with preheat roll, and the bottom is provided with side discharging transit network belt drive roller; Described heating clamber is divided into two-layer up and down, and the upper strata is provided with heat resisting steel Muffle pot and burner, and lower floor is provided with heat-resisting carrying roller; Described water steam chamber top is provided with live-roller and idler roller, and the bottom is provided with carrying roller, and the top is provided with the water vapour floss hole; Described guipure naturally extends and is provided with side discharging switching guipure driven roller and backing roll in trench;
Described transport network band is around described feeder, material loading deflector roll, preheat roll, live-roller and idler roller, and described heating clamber is passed in the centre;
Described side discharging transit network band is around described side discharging transit network belt drive roller, heat-resisting carrying roller, side discharging switching guipure driven roller and backing roll, and described heating clamber and described water steam chamber are passed in the centre.
Preferably, described heating clamber top is provided with the steam suction inlet.
Preferably, the inboard discharging switching guipure of described heating clamber below is provided with heavy remaining plaster cleaning guipure.
Preferably, described preheating chamber top is provided with cold-hot wind exchange blower fan.
Preferably, be provided with blow tank bottom described preheating chamber.
Preferably, described water steam chamber top is provided with the steam blower fan that draws water.
Preferably, close described heating clamber place, described water steam chamber top is provided with the tail gas burner.
Can find out from above-mentioned technical scheme, a kind of continuous transfer sludge incineration caking stove disclosed in this invention, by being provided with preheating chamber at heating clamber one end, the other end is provided with water steam chamber, the high-temperature flue gas that produces after burning is transported to preheating chamber wet mud is first carried out the pre-heating temperature elevation drying, and the water vapour that produces is in time processed, thereby be able to make UTILIZATION OF VESIDUAL HEAT IN, energy savings and burn effective purpose.
Description of drawings
In order to be illustrated more clearly in the embodiment of the present invention or technical scheme of the prior art, the below will do to introduce simply to the accompanying drawing of required use in embodiment or description of the Prior Art, apparently, accompanying drawing in the following describes is only some embodiments of the present invention, for those of ordinary skills, under the prerequisite of not paying creative work, can also obtain according to these accompanying drawings other accompanying drawing;
Fig. 1 is the disclosed a kind of continuous transfer sludge incineration caking furnace structure schematic diagram of the embodiment of the present invention.
The title of the corresponding component that the numeral in figure or letter are represented:
11, support 12, feeder 13, material loading deflector roll 2, transmit guipure 3, preheating chamber 31, floss hole 32, preheat roll 33, side discharging transit network belt drive roller 34, cold-hot wind exchange blower fan 35, blow tank 4, heating clamber 41, heat resisting steel Muffle pot 42, burner 43, heat-resisting carrying roller 44, steam suction inlet 5, water steam chamber 51, live-roller 52, idler roller 53, carrying roller 54, water vapour floss hole 55, steam blower fan 6 draws water, side discharging switching guipure 7, guipure extends trench 71 naturally, side discharging switching guipure driven roller 72, backing roll 8, heavy remaining plaster cleaning guipure 9, the tail gas burner
The specific embodiment
Below in conjunction with accompanying drawing, the technical scheme in the embodiment of the present invention is clearly and completely described, obviously, described embodiment is only the present invention's part embodiment, rather than whole embodiment.Based on the embodiment in the present invention, those of ordinary skills are not making the every other embodiment that obtains under the creative work prerequisite, all belong to the scope of protection of the present invention.
The invention discloses a kind of continuous transfer sludge incineration caking stove, make UTILIZATION OF VESIDUAL HEAT IN, energy savings and burn effective purpose being able to.
Embodiment.
As shown in Figure 1, a kind of continuous transfer sludge incineration caking stove comprises that feeding device, transmission guipure 2, system of bf body, side discharging switching guipure 6 and guipure extend trench 7 naturally;
Described feeding device comprises support 11, feeder 12 and material loading deflector roll 13; Described system of bf body comprises preheating chamber 3, heating clamber 4 and water steam chamber 5; Described preheating chamber 3 tops are provided with floss hole 31 and cold-hot wind exchange blower fan 34, and top is provided with preheat roll 32, and the bottom is provided with side discharging transit network belt drive roller 33, and the bottom is provided with blow tank 35; Described heating clamber 4 is divided into two-layer up and down, and the upper strata is provided with heat resisting steel Muffle pot 41 and burner 42, and lower floor is provided with heat-resisting carrying roller 43, and the top is provided with steam suction inlet 44; Described water steam chamber 5 tops are provided with live-roller 51 and idler roller 52, and the bottom is provided with carrying roller 53, and the top is provided with water vapour floss hole 54 and the steam blower fan 55 that draws water; Described guipure naturally extends and is provided with side discharging switching guipure driven roller 71 and backing roll 72 in trench 7;
Described transmission guipure 2 is around described feeder 12, material loading deflector roll 13, preheat roll 32, live-roller 51 and idler roller 52, and described heating clamber 4 is passed in the centre;
Described side discharging switching guipure 6 is around described side discharging transit network belt drive roller 33, heat-resisting carrying roller 43, side discharging switching guipure driven roller 71 and backing roll 72, and described heating clamber 4 and described water steam chamber 5 are passed in the centre.
Wherein, described heating clamber 4 private side dischargings switching guipure 6 belows are provided with heavy remaining plaster cleaning guipure 8; Close described heating clamber 4 places, described water steam chamber 5 tops are provided with tail gas burner 9.
The production process of a kind of continuous transfer sludge incineration caking stove of the present invention is as follows: at first wet mud is positioned on the top transmission guipure 2 of feeder 12, then be sent in preheating chamber 3, because the interior string of preheating chamber 3 has from the high-temperature flue gas in heating clamber 4, therefore, the wet mud of this moment is processed by preliminarily dried, when entering heating clamber 4 again, moisture has evaporated a part, and the water vapour of evaporation is discharged from floss hole 31 by cold-hot wind exchange blower fan 34.Then the mud after the pre-heat treatment is transmitted guipure 2 and is sent to and carries out finish-drying in heating clamber 4, this moment due to wet mud from heat resisting steel Muffle pot 41 and burner 42 close to, can produce a large amount of water vapours, so it is cooling to be sucked cooling chambers by the steam suction inlet 44 from heating clamber 4 tops, it is further cooling that mud after final drying is admitted to water steam chamber 5, water vapour is herein drawn water steam blower fan 55 from 54 discharges of water vapour floss hole, if the oil smoke or the combustible gas concentration that produce can be burnt it by tail gas burner 9 more greatly.The sludge-drying of this moment can drop on side discharging switching guipure 6 from transmitting guipure 2, then is transported to blow tank 35 places by side discharging switching guipure 6, has both obtained the mud of drying and incinerating caking.
Can find out from above-mentioned technical scheme, a kind of continuous transfer sludge incineration caking stove disclosed in this invention, by being provided with preheating chamber 3 at heating clamber 4 one ends, the other end is provided with water steam chamber 5, the high-temperature flue gas that produces after burning is transported to 3 pairs of wet mud of preheating chamber first carries out the pre-heating temperature elevation drying, and the water vapour that produces is in time discharged, thereby be able to make UTILIZATION OF VESIDUAL HEAT IN, energy savings and burn effective purpose.
Be more than to the description of a kind of continuous transfer sludge incineration caking of the present invention stove embodiment, by the above-mentioned explanation to the disclosed embodiments, make this area professional and technical personnel can realize or use the present invention.Multiple modification to these embodiment will be apparent concerning those skilled in the art, and General Principle as defined herein can be in the situation that do not break away from the spirit or scope of the present invention, realization in other embodiments.Therefore, the present invention will can not be restricted to these embodiment shown in this article, but will meet the widest scope consistent with principle disclosed herein and features of novelty.
Claims (7)
1. a continuous transfer sludge incineration caking stove, is characterized in that, comprises that feeding device, transmission guipure, system of bf body, side discharging switching guipure and guipure extend trench naturally;
Described feeding device comprises support, feeder and material loading deflector roll; Described system of bf body comprises preheating chamber, heating clamber and water steam chamber; Described preheating chamber top is provided with floss hole, and top is provided with preheat roll, and the bottom is provided with side discharging transit network belt drive roller; Described heating clamber is divided into two-layer up and down, and the upper strata is provided with heat resisting steel Muffle pot and burner, and lower floor is provided with heat-resisting carrying roller; Described water steam chamber top is provided with live-roller and idler roller, and the bottom is provided with carrying roller, and the top is provided with the water vapour floss hole; Described guipure naturally extends and is provided with side discharging switching guipure driven roller and idler roller in trench;
Described transport network band is around described feeder, material loading deflector roll, preheat roll, live-roller and idler roller, and described heating clamber is passed in the centre;
Described side discharging transit network band is around described side discharging transit network belt drive roller, heat-resisting carrying roller, side discharging switching guipure driven roller and idler roller, and described heating clamber and described water steam chamber are passed in the centre.
2. a kind of continuous transfer sludge incineration caking stove according to claim 1, is characterized in that, described heating clamber top is provided with the steam suction inlet.
3. a kind of continuous transfer sludge incineration caking stove according to claim 2, is characterized in that, is provided with heavy remaining plaster cleaning guipure below described heating clamber private side discharging switching guipure.
4. a kind of continuous transfer sludge incineration caking stove according to claim 1, is characterized in that, described preheating chamber top is provided with cold-hot wind exchange blower fan.
5. a kind of continuous transfer sludge incineration caking stove according to claim 1, is characterized in that, described preheating chamber bottom is provided with blow tank.
6. a kind of continuous transfer sludge incineration caking stove according to claim 1, is characterized in that, described water steam chamber top is provided with the steam blower fan that draws water.
7. a kind of continuous transfer sludge incineration caking stove according to claim 1, is characterized in that, close described heating clamber place, described water steam chamber top is provided with the tail gas burner.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011104196243A CN103162300A (en) | 2011-12-15 | 2011-12-15 | Continuous type transmission sludge burning caking furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011104196243A CN103162300A (en) | 2011-12-15 | 2011-12-15 | Continuous type transmission sludge burning caking furnace |
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| CN103162300A true CN103162300A (en) | 2013-06-19 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2011104196243A Pending CN103162300A (en) | 2011-12-15 | 2011-12-15 | Continuous type transmission sludge burning caking furnace |
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Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105906177A (en) * | 2016-06-30 | 2016-08-31 | 安徽未名鼎和环保有限公司 | Sludge treatment facility |
| CN105927989A (en) * | 2016-06-30 | 2016-09-07 | 安徽未名鼎和环保有限公司 | Pretreatment type sludge incineration treatment system |
| CN105927988A (en) * | 2016-06-30 | 2016-09-07 | 安徽未名鼎和环保有限公司 | Efficient sludge incineration treatment system |
| CN105923955A (en) * | 2016-06-30 | 2016-09-07 | 安徽未名鼎和环保有限公司 | Efficient moisture-removing type sludge treatment device |
| CN105923979A (en) * | 2016-06-30 | 2016-09-07 | 安徽未名鼎和环保有限公司 | High-efficient sludge processing device |
| CN105972616A (en) * | 2016-06-30 | 2016-09-28 | 安徽未名鼎和环保有限公司 | Efficient energy-saving sludge treatment device |
| CN105972612A (en) * | 2016-06-30 | 2016-09-28 | 安徽未名鼎和环保有限公司 | Efficient and fast sludge treatment equipment |
| CN105972615A (en) * | 2016-06-30 | 2016-09-28 | 安徽未名鼎和环保有限公司 | Combustion type sludge treatment device |
| CN106016298A (en) * | 2016-06-30 | 2016-10-12 | 安徽未名鼎和环保有限公司 | Sludge incineration treatment system |
| CN106016300A (en) * | 2016-06-30 | 2016-10-12 | 安徽未名鼎和环保有限公司 | Low-energy-consumption and low-pollution sludge treatment device |
| CN106051788A (en) * | 2016-06-30 | 2016-10-26 | 安徽未名鼎和环保有限公司 | Sludge sufficient combustion processing device |
| CN106122978A (en) * | 2016-06-30 | 2016-11-16 | 安徽未名鼎和环保有限公司 | A kind of preheating type Disposal System of Mud Burning |
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Cited By (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105906177A (en) * | 2016-06-30 | 2016-08-31 | 安徽未名鼎和环保有限公司 | Sludge treatment facility |
| CN105927989A (en) * | 2016-06-30 | 2016-09-07 | 安徽未名鼎和环保有限公司 | Pretreatment type sludge incineration treatment system |
| CN105927988A (en) * | 2016-06-30 | 2016-09-07 | 安徽未名鼎和环保有限公司 | Efficient sludge incineration treatment system |
| CN105923955A (en) * | 2016-06-30 | 2016-09-07 | 安徽未名鼎和环保有限公司 | Efficient moisture-removing type sludge treatment device |
| CN105923979A (en) * | 2016-06-30 | 2016-09-07 | 安徽未名鼎和环保有限公司 | High-efficient sludge processing device |
| CN105972616A (en) * | 2016-06-30 | 2016-09-28 | 安徽未名鼎和环保有限公司 | Efficient energy-saving sludge treatment device |
| CN105972612A (en) * | 2016-06-30 | 2016-09-28 | 安徽未名鼎和环保有限公司 | Efficient and fast sludge treatment equipment |
| CN105972615A (en) * | 2016-06-30 | 2016-09-28 | 安徽未名鼎和环保有限公司 | Combustion type sludge treatment device |
| CN106016298A (en) * | 2016-06-30 | 2016-10-12 | 安徽未名鼎和环保有限公司 | Sludge incineration treatment system |
| CN106016300A (en) * | 2016-06-30 | 2016-10-12 | 安徽未名鼎和环保有限公司 | Low-energy-consumption and low-pollution sludge treatment device |
| CN106051788A (en) * | 2016-06-30 | 2016-10-26 | 安徽未名鼎和环保有限公司 | Sludge sufficient combustion processing device |
| CN106122978A (en) * | 2016-06-30 | 2016-11-16 | 安徽未名鼎和环保有限公司 | A kind of preheating type Disposal System of Mud Burning |
| CN105927989B (en) * | 2016-06-30 | 2018-11-13 | 安徽未名鼎和环保有限公司 | A kind of pretreatment type Disposal System of Mud Burning |
| CN106016298B (en) * | 2016-06-30 | 2018-11-13 | 安徽未名鼎和环保有限公司 | A kind of Disposal System of Mud Burning |
| CN106016300B (en) * | 2016-06-30 | 2018-12-07 | 安徽未名鼎和环保有限公司 | A kind of sludge treatment equipment of low energy consumption low pollution |
| CN105972616B (en) * | 2016-06-30 | 2018-12-07 | 安徽未名鼎和环保有限公司 | A kind of sludge energy-saving processing unit |
| CN105972612B (en) * | 2016-06-30 | 2018-12-07 | 安徽未名鼎和环保有限公司 | A kind of equipment of quick processing sludge |
| CN106122978B (en) * | 2016-06-30 | 2019-01-08 | 安徽未名鼎和环保有限公司 | A kind of preheating type Disposal System of Mud Burning |
| CN105906177B (en) * | 2016-06-30 | 2019-04-05 | 安徽未名鼎和环保有限公司 | A kind of sludge treatment device |
| CN105923955B (en) * | 2016-06-30 | 2019-04-09 | 安徽未名鼎和环保有限公司 | It is a kind of efficiently to remove moisture type sludge treatment device |
| CN105923979B (en) * | 2016-06-30 | 2019-04-09 | 安徽未名鼎和环保有限公司 | A kind of sludge high-efficient treatment device |
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Application publication date: 20130619 |