CN206919020U - A kind of vertical rotating pyrogenation incinerator of composite ring air inlet and discharge gate - Google Patents

A kind of vertical rotating pyrogenation incinerator of composite ring air inlet and discharge gate Download PDF

Info

Publication number
CN206919020U
CN206919020U CN201720435871.5U CN201720435871U CN206919020U CN 206919020 U CN206919020 U CN 206919020U CN 201720435871 U CN201720435871 U CN 201720435871U CN 206919020 U CN206919020 U CN 206919020U
Authority
CN
China
Prior art keywords
rotary barrel
funnel
interlayer
scum pipe
air
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201720435871.5U
Other languages
Chinese (zh)
Inventor
彭跃进
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Peng Yuejin
Original Assignee
Wutongqiao District Of Leshan City Jia Chuan Machinery Manufacturing Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Wutongqiao District Of Leshan City Jia Chuan Machinery Manufacturing Co Ltd filed Critical Wutongqiao District Of Leshan City Jia Chuan Machinery Manufacturing Co Ltd
Priority to CN201720435871.5U priority Critical patent/CN206919020U/en
Application granted granted Critical
Publication of CN206919020U publication Critical patent/CN206919020U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The vertical rotating pyrogenation incinerator of composite ring air inlet and discharge gate described in the utility model, combustion chamber including top and the funnel-form scum pipe below combustion chamber, osculum below the funnel-form scum pipe is connected with rotary barrel, the side wall of the rotary barrel and funnel-form scum pipe is provided with hollow interlayer, air outlet is provided with the top of interlayer, rotary barrel side wall interlayer is connected with horizontal airduct, and horizontal airduct is connected with air inlet.The utility model is eliminated in the past positioned at the airduct in rotary barrel and funnel-form scum pipe center, so as to expand deslagging open area, avoids slag-drip opening from blocking;Using annular air structure, air-out path and air-out direction change in the past relatively, and reduction dust, which is impacted, is upwardly into top of combustion chamber exhaust duct, it is no longer deposited in exhaust duct.

Description

A kind of vertical rotating pyrogenation incinerator of composite ring air inlet and discharge gate
Technical field
The utility model belongs to mechanical field, is related to a kind of waste incinerator, and in particular to a kind of composite ring air inlet With the vertical rotating pyrogenation incinerator of discharge gate.
Background technology
Existing vertical-type garbage incinerator air inlet is with slag-drip opening typical structure as shown in figure 3, vertical airduct 9 is straight by bottom Upper to be entered by rotary barrel, funnel-form scum pipe in combustion chamber, the wind-force at center is maximum, and blast is revolved by dying down by force with edge The clinker that drum body falls is liquidated, and less clinker can be then again introduced into combustion chamber with the wind, causes to arrange on incinerator top Dust in the flue gas gone out is more, is condensed again after influenceing the combustion efficiency of second-time burning and the thawing of dust, causes the stifled of flue Plug;Second, usually there is industrial refuse in rubbish(Such as steel wire, building waste), due to the limitation of incineration temperature(Maximum temperature one As control in the range of 1200 °), do not change the solid forms in rubbish;Blast pipe is among rotary barrel in existing structure Position, slag-drip opening are a ring-shaped, and blast pipe occupies deslagging space, easily cause rotary barrel not have because deslagging space is limited Pre-process the rubbish decomposed to accumulate in slag-drip opening, can not discharge, slag-drip opening blocking is ultimately resulted in, to whole refuse burning system band Carrying out system can not run and shutdown maintenance, and the workload overhauled is very big.
Utility model content
To overcome existing vertical-type garbage incinerator air inlet structure to cause slag-drip opening easily to block, and air quantity is larger causes dust Raise up, liquefied into combustion chamber, in the technological deficiency of exhaust outlet cooling and solidifying deposition, the utility model discloses a kind of complex loop The vertical rotating pyrogenation incinerator of shape air inlet and discharge gate.
The vertical rotating pyrogenation incinerator of composite ring air inlet and discharge gate described in the utility model, includes the combustion of top Burning room and the funnel-form scum pipe below combustion chamber, the osculum below the funnel-form scum pipe is connected with rotary barrel, The side wall of the rotary barrel and funnel-form scum pipe is provided with hollow interlayer, and air outlet, rotating cylinder are provided with the top of interlayer Body sidewall interlayer is connected with horizontal airduct, and horizontal airduct is connected with air inlet.
Preferably, the rotary barrel side wall position relative with horizontal airduct is provided with air intake dsah-pot.
Preferably, it is provided with solid waste conveyer belt below the rotary barrel.
Preferably, the junction of the horizontal airduct and rotary barrel side wall interlayer is provided with a bore contraction section.
Using composite ring air inlet described in the utility model and the vertical rotating pyrogenation incinerator of discharge gate, possess as Lower superiority:
Effective deslagging area of one, vertical incinerator slag-drip openings is increased, and so as to be advantageous to the deslagging of total system, is burnt Solid forms rubbish residue after burning will not at slag-drip opening accumulated plugging slag-drip opening, enable the effective deslagging of incinerator and make Deslagging is more effectively smooth, so as to greatly prolong the separate run times of incinerator, its incinerator operational efficiency is improved and is run Cost is reduced.
Two, increase air-out open area, reduce blast, and are changed into the low blast of surrounding from the high blast in original middle part, this Sample is more beneficial for the abundant burning in incinerator, makes to enter the air in incinerator and the clinker of whereabouts in stove is no longer directly right Punching, so as to reduce the finely ground particles in the air for entering incineration section, incineration section is set more fully to burn.
Three, the utility model are effectively improved the pressure of air outlet in stove, increase the effective area of air outlet, are advantageous to reach The requirement of Wind Volume, low-head to incinerator design requirement, be advantageous to incinerator operation control, reduce into burning Dust in the exhaust duct of room, it is no longer cooled down and be deposited in exhaust duct.
Four, make full use of the characteristic that slag-drip opening is embedded in deslagging cooling water, between making between rotary barrel and intake stack Gap also reduces manufacturing cost because the effect of water reaches sealing function.
Brief description of the drawings
Fig. 1 be vertical rotating pyrogenation incinerator described in the utility model a kind of embodiment structural representation, Fig. 2 For the schematic side view of embodiment shown in vertical rotating pyrogenation incinerator Fig. 1 described in the utility model, Fig. 3 is existing skill The structural representation of vertical rotating pyrogenation incinerator in art;The entitled 1- combustion chambers of reference in figure, 2- funnel-form scum pipes, The horizontal airducts of 3-, 4- air inlets, 5- rotary barrel side walls, 6- interlayers, 7- air outlets, 8- rotary barrels, the vertical airducts of 9-, 10- Unmarked arrow represents solid waste outbound course in air intake dsah-pot, Fig. 2 and Fig. 3, and wave represents the water surface.
Embodiment
Below in conjunction with the accompanying drawings, specific embodiment of the present utility model is described in further detail.
The vertical rotating pyrogenation incinerator of composite ring air inlet and discharge gate described in the utility model, as shown in figure 1, bag Include the combustion chamber of top and the funnel-form scum pipe 2 positioned at the lower section of combustion chamber 1, osculum and rotation below the funnel-form scum pipe Drum body connects, and the side wall of the rotary barrel 8 and funnel-form scum pipe is provided with hollow interlayer 6, is provided with the top of interlayer Air outlet 7, the interlayer of rotary barrel side wall 5 are connected with horizontal airduct 3, and horizontal airduct is connected with air inlet 4.
When setting up, funnel-form scum pipe and combustion chamber are usually located at more than ground vertical incinerator, and lower section is provided with water Pond, rotary barrel and air inlet system are all disposed within underwater, carry out the sealing of air intake duct and solid particulate matter with water, Fig. 2 and Corrugated curve in Fig. 3 represents waterline.
In use, air inlet is connected with blower fan, blown by horizontal airduct into interlayer, the rotary barrel of air-flow from below Interlayer flows into the funnel-form scum pipe interlayer of top, is then sprayed from the air outlet at the top of interlayer to combustion chamber.The utility model Eliminate in the past positioned at the airduct in rotary barrel and funnel-form scum pipe center, so as to expand deslagging open area, burn and produce Solid slag dropped from the whole cross section of rotary barrel, will not be blocked in conventional annular slag-drip opening, fall directly into and set Underwater conveyer belt is put, solid slag is all sent out.
Meanwhile changed in the past relatively using annular air structure, air-out path and air-out direction, no longer it is straight up Air-flow, but sprayed from interlayer into combustion chamber, so as to not liquidated with the direction that dust falls vertically, reduce dust and rushed Hit and be upwardly into top of combustion chamber exhaust duct, it is no longer accumulated in exhaust duct rapidly.
Using composite ring air inlet described in the utility model and the vertical rotating pyrogenation incinerator of discharge gate, possess as Lower superiority:
Effective deslagging area of one, vertical incinerator slag-drip openings is increased, and so as to be advantageous to the deslagging of total system, is burnt Solid forms rubbish residue after burning will not at slag-drip opening accumulated plugging slag-drip opening, enable the effective deslagging of incinerator and make Deslagging is more effectively smooth, so as to greatly prolong the separate run times of incinerator, its incinerator operational efficiency is improved and is run Cost is reduced.
Two, increase air-out open area, reduce blast, and are changed into the low blast of surrounding from the high blast in original middle part, this Sample is more beneficial for the abundant burning in incinerator, makes to enter the air in incinerator and the clinker of whereabouts in stove is no longer directly right Punching, so as to reduce the finely ground particles in the air for entering incineration section, incineration section is set more fully to burn.
Three, the utility model are effectively improved the pressure of air outlet in stove, increase the effective area of air outlet, are advantageous to reach The requirement of Wind Volume, low-head to incinerator design requirement, be advantageous to incinerator operation control, reduce into burning Dust in the exhaust duct of room, it is no longer cooled down and be deposited in exhaust duct.
Four, make full use of the characteristic that slag-drip opening is embedded in deslagging cooling water, between making between rotary barrel and intake stack Gap also reduces manufacturing cost because the effect of water reaches sealing function.
In embodiment shown in Fig. 1, the rotary barrel side wall position relative with horizontal airduct be provided with into Wind dsah-pot 10, be advantageous to be upwardly formed the updraft of stable and uniform in the week of interlayer..
Solid waste conveyer belt is provided with below the rotary barrel, as shown in Fig. 2 backwardness is collected under solid waste On conveyer belt, the water surface is taken out of with the direction shown in Fig. 2 by conveyer belt, Fig. 2 visual angle is with rotary barrel axial-rotation in Fig. 1 Visual angle profile obtained by 90 degree.
One bore contraction section can be set in the junction of horizontal airduct and rotary barrel side wall interlayer, to interlayer direction Bore shrinks, so as to improve into interlayer wind speed and amendment wind direction.
Using congee pot described in the utility model, the communication of the forms such as satellite voice, short message and Email can be provided Service.The product can be used for the specific communication field such as disaster relief, emergency communication, media report, exploration and scientific investigation, and communicate into This is cheap.
Previously described is each preferred embodiment of the present utility model, the preferred embodiment in each preferred embodiment If not obvious contradictory or premised on a certain preferred embodiment, each preferred embodiment can be arbitrarily superimposed It is applied in combination, the design parameter in the embodiment and embodiment is merely to clearly state the utility model of utility model people Verification process, and be not used to limit scope of patent protection of the present utility model, scope of patent protection of the present utility model still with Its claims is defined, every equivalent structure change made with specification of the present utility model and accompanying drawing content, similarly It should be included in the scope of protection of the utility model.

Claims (4)

  1. A kind of 1. vertical rotating pyrogenation incinerator of composite ring air inlet and discharge gate, it is characterised in that:Combustion including top Burning room and the funnel-form scum pipe below combustion chamber, the osculum below the funnel-form scum pipe is connected with rotary barrel, The side wall of the rotary barrel and funnel-form scum pipe is provided with hollow interlayer, and air outlet, rotating cylinder are provided with the top of interlayer Body sidewall interlayer is connected with horizontal airduct, and horizontal airduct is connected with air inlet.
  2. 2. vertical rotating pyrogenation incinerator as claimed in claim 1, it is characterised in that the rotary barrel side wall and horizontal wind Manage relative position and be provided with air intake dsah-pot.
  3. 3. vertical rotating pyrogenation incinerator as claimed in claim 1, it is characterised in that be provided with below the rotary barrel solid Body scrap conveyor.
  4. 4. vertical rotating pyrogenation incinerator as claimed in claim 1, it is characterised in that the horizontal airduct and rotating cylinder side The junction of wall interlayer is provided with a bore contraction section.
CN201720435871.5U 2017-04-25 2017-04-25 A kind of vertical rotating pyrogenation incinerator of composite ring air inlet and discharge gate Expired - Fee Related CN206919020U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720435871.5U CN206919020U (en) 2017-04-25 2017-04-25 A kind of vertical rotating pyrogenation incinerator of composite ring air inlet and discharge gate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720435871.5U CN206919020U (en) 2017-04-25 2017-04-25 A kind of vertical rotating pyrogenation incinerator of composite ring air inlet and discharge gate

Publications (1)

Publication Number Publication Date
CN206919020U true CN206919020U (en) 2018-01-23

Family

ID=61305958

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720435871.5U Expired - Fee Related CN206919020U (en) 2017-04-25 2017-04-25 A kind of vertical rotating pyrogenation incinerator of composite ring air inlet and discharge gate

Country Status (1)

Country Link
CN (1) CN206919020U (en)

Similar Documents

Publication Publication Date Title
CN211695832U (en) Vertical cement clinker pneumatic particle grading cooler
CN207762914U (en) A kind of fluid bed solids trash burner
CN204313270U (en) A kind of biomass shaped fuel boiler
CN104121585A (en) Rubbish incineration and waste gas purification device and feeding machine thereof
CN206919020U (en) A kind of vertical rotating pyrogenation incinerator of composite ring air inlet and discharge gate
CN107842850B (en) A kind of fluidized bed combustor
CN206973578U (en) A kind of different fluidized bed refuse incinerator that recirculates
CN103787391B (en) A kind of new dry process equipment for the production of flyash alumina clinker
CN102424887A (en) Gas drying type dust removal system of converter
CN108686839B (en) High-efficient cyclone that purifies
CN203791071U (en) Volute cyclone dust collector
CN201880849U (en) Discharging device of casting waste sand roasting furnace
CN210400023U (en) Hollow brick production system with waste heat recycling function
CN201756361U (en) Dust removal emptying machine set
CN114294652A (en) Be used for discarded object broken combustion processing apparatus
CN203571756U (en) Garbage burning and exhaust gas purifier
CN210241545U (en) Biomass combustion boiler
CN201470239U (en) Slag micro powder bag dust collector
CN112240710A (en) Vertical flow annular cooler for cement clinker
CN206724220U (en) The feed hopper of novel biomass fuel boiler
CN220817749U (en) Garbage high-temperature cracking furnace
CN211176815U (en) Miniature domestic refuse treating furnace
CN220771124U (en) Inner furnace core for garbage treatment heat balance high-temperature cracking furnace
CN218723049U (en) Kiln body with high thermal efficiency
CN213930959U (en) Kiln tail ash discharge air sealing device

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20180412

Address after: 610000 No. 1, unit 1, No. 1233, Li Li Road, Jinjiang District, Chengdu, Sichuan 1704

Patentee after: Peng Yuejin

Address before: 614000 Miu Ba village, Niu Hua Town, Leshan, Sichuan

Patentee before: Wutongqiao District of Leshan City Jia Chuan Machinery Manufacturing Co. Ltd.

TR01 Transfer of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20180123

Termination date: 20180425

CF01 Termination of patent right due to non-payment of annual fee