CN107255281A - A kind of powder continuous heat system - Google Patents
A kind of powder continuous heat system Download PDFInfo
- Publication number
- CN107255281A CN107255281A CN201710528798.0A CN201710528798A CN107255281A CN 107255281 A CN107255281 A CN 107255281A CN 201710528798 A CN201710528798 A CN 201710528798A CN 107255281 A CN107255281 A CN 107255281A
- Authority
- CN
- China
- Prior art keywords
- transfer pipe
- axle
- charging aperture
- air inlet
- driving motor
- 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.)
- Pending
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
- F23G5/0276—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage using direct heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/033—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment comminuting or crushing
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/442—Waste feed arrangements
- F23G5/444—Waste feed arrangements for solid waste
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The invention provides a kind of powder continuous heat system, including feeding warehouse, screw feeding axle, driving motor, Transfer pipe, high temperature process furnances, recovery bin, air inlet, gas outlet；Wherein the rotary shaft of screw feeding axle and driving motor is connected and rotated under the driving of rotary shaft around itself axle, Transfer pipe is fixedly connected with screw feeding axle and passes through high temperature process furnances, the feeding port of feeding warehouse is connected with the charging aperture of Transfer pipe, the charging aperture of recovery bin is connected with the discharging opening of Transfer pipe, air inlet is arranged near the charging aperture of Transfer pipe, and gas outlet is arranged near the discharging opening of Transfer pipe.
Description
Technical field
The present invention relates to a kind of mechanical device being continuously driven and high-temperature heat treatment technology, particularly a kind of powder Continuous Heat
Processing system.
Background technology
The mode of boiler burning disposal is usually taken in modern industry for the powder in some coal dusts and discarded object, this
Many organic matters containing contaminative in a little coal dusts and rubbish, can produce a large amount of pernicious gases, it is not easy to receive in burning process
Collection, does not allow disposable yet.Meanwhile, this kind of material is burned because oxidizing fire is insufficient, can produce substantial amounts of soot, these soots
Particle is attached on inboard wall of burner hearth, and the time is more long, and deposition is bigger, can influence the efficiency of burner hearth, it is therefore desirable to periodic cleaning, and ten
Divide inconvenience.
Pyrolysis is as a kind of processing mode different from commonly burning, and it, which is distinguished, essentially consists in pyrolytic process without obvious
Flame, and the temperature of thermal process reactor can be controlled, the material finally produced is also had nothing in common with each other.It can be generated after common burning
The toxic gases such as carbon monoxide, bioxin；Substantial amounts of carbon dioxide and the solid matter of melting.The process of pyrolysis processing,
Easy to operate and safe, service life is long, and the dust content of generation is low, therefore will not produce substantial amounts of jet-black, but can generate
Tarry matters, present pyrolysis processing, which is primarily present, to be not easy to recuperation of heat, big, the automatic control level requirement height of refractory material influence etc. and lacks
Point.
The content of the invention
It is an object of the invention to provide a kind of powder continuous heat system, including feeding warehouse, screw feeding axle, transmission
Motor, Transfer pipe, high temperature process furnances, recovery bin, air inlet, gas outlet；The wherein rotation of screw feeding axle and driving motor
Axle is connected and rotated under the driving of rotary shaft around itself axle, and Transfer pipe is fixedly connected with screw feeding axle and passes through high temperature pipe
Formula stove, the feeding port of feeding warehouse is connected with the charging aperture of Transfer pipe, and the charging aperture of recovery bin and the discharging opening of Transfer pipe connect
Logical, air inlet is arranged near the charging aperture of Transfer pipe, and gas outlet is arranged near the discharging opening of Transfer pipe.
Using said system, driving motor rotating speed is adjustable.
The present invention is reacted discarded object feeding high temperature process furnances by the way of swivel feeding, and powder can be carried out
Continuously handle, and the residue and oily mater that can be effectively discharged out producing in heat treatment process avoid causing the stifled of boiler tube
Plug；Swivel feeding can cause discarded object sufficient oxidizing fire in high temperature process furnances；Set simultaneously in the end of Transfer pipe
Recovery bin is put to reclaim reacted material.
The present invention is described further with reference to Figure of description.
Brief description of the drawings
Fig. 1 is structural representation of the invention.
Embodiment
With reference to Fig. 1, a kind of powder continuous heat system, including feeding warehouse 1, screw feeding axle 3, driving motor 2, transmission
Passage 9, high temperature process furnances 4, recovery bin 7, air inlet 8, gas outlet 6；The wherein rotary shaft of screw feeding axle 3 and driving motor 2
Connect and rotated under the driving of rotary shaft around itself axle, Transfer pipe 9 is fixedly connected with screw feeding axle 3 and passes through high temperature pipe
Formula stove 4, the feeding port of feeding warehouse 1 is connected with the charging aperture of Transfer pipe 9, the charging aperture of recovery bin 7 and the discharging of Transfer pipe 9
Mouth connection, air inlet 8 is arranged near the charging aperture of Transfer pipe 9, and gas outlet 6 is arranged near the discharging opening of Transfer pipe 9.
Screw feeding axle 3, driving motor 2, Transfer pipe 9 are used for promoting powder to move with certain speed.
System also includes pulverizer, and the pulverizer is transmitted to feeding warehouse 1, after crushing after the organic waste of bulk is crushed
Powdered substance it is easily decomposes.
System also includes pressure gauge 5, the pressure near discharging opening for measuring Transfer pipe 9.
Air inlet 8 is used to be passed through oxygen.
The rotating speed of driving motor 2 is adjustable, by changing speed the powder in high temperature process furnances 4 can be allowd abundant
Carry out oxidation reaction.
A large amount of powders are mounted in the larger feeding warehouse 1 of a volume in advance, feeding warehouse 1 and underlying Transfer pipe 9, and
With the turnover that dividing plate is switch control powder.The inside of Transfer pipe 9 is equipped with a screw feeding axle 3 through Overheating Treatment, and axle is left
Side is connected with driving motor 2, the speed for changing the rotating speed of feed spool by the power of controlled motor and then controlling powder to advance.Together
When Transfer pipe 9 middle body be in tube furnace 4 bringing-up section, when powder with the rotation of helical axis be moved to boiler tube center
When, powder is thermally decomposed at high temperature, reaches the purpose of heat treatment.Powder by thermal decomposition can form the thing of tarry
Matter, under the impetus of helical axis and powder, moves to the right side afterbody of Transfer pipe 9.There is an opening in afterbody, after heat treatment
Powder and the tarry matters formed fall into the powder recovery bin 7 of lower section by opening.Meanwhile, Transfer pipe 9 is used as heat treatment
The main part of system, the left and right sides is completely enclosed, and is each side extended with an aperture, respectively air inlet 8 and gas outlet
6, air inlet 8 is passed through oxygen, and as the reacting gas of heat treatment, the connecting line of gas outlet 6 discharges the waste gas of generation.
Claims (7)
1. a kind of powder continuous heat system, it is characterised in that including feeding warehouse (1), screw feeding axle (3), driving motor
(2), Transfer pipe (9), high temperature process furnances (4), recovery bin (7), air inlet (8), gas outlet (6)；Wherein
Screw feeding axle (3) is connected with the rotary shaft of driving motor (2) and rotated under the driving of rotary shaft around itself axle,
Transfer pipe (9) is fixedly connected with screw feeding axle (3) and through high temperature process furnances (4),
The feeding port of feeding warehouse (1) is connected with the charging aperture of Transfer pipe (9),
The charging aperture of recovery bin (7) is connected with the discharging opening of Transfer pipe (9),
Air inlet (8) is arranged near the charging aperture of Transfer pipe (9),
Gas outlet (6) is arranged near the discharging opening of Transfer pipe (9).
2. system according to claim 1, it is characterised in that system also includes pulverizer, the pulverizer has bulk
Machine discarded object is transmitted to feeding warehouse (1) after crushing.
3. system according to claim 1, it is characterised in that system also includes pressure gauge (5), for measuring Transfer pipe
(9) the pressure near discharging opening.
4. system according to claim 1, it is characterised in that air inlet (8) is used to be passed through oxygen.
5. system according to claim 1, it is characterised in that driving motor (2) rotating speed is adjustable.
6. system according to claim 1, it is characterised in that Transfer pipe (9) is metal tube.
7. system according to claim 1, it is characterised in that the relevant parameter of the system is as follows：
Motor maximal input：7kW
Maximum operation (service) temperature：1000℃
Temperature-controlled precision：±1℃
Heating zone length：900mm
Constant temperature section length：550mm
Boiler tube size：Φ50*1800mm
Furnace tube material：310S stainless steel tubes
Cold conditions is pressure-resistant：2Mpa
Feed storage bin size：8L
Powder recovery bin size：5L.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710528798.0A CN107255281A (en) | 2017-07-01 | 2017-07-01 | A kind of powder continuous heat system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710528798.0A CN107255281A (en) | 2017-07-01 | 2017-07-01 | A kind of powder continuous heat system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107255281A true CN107255281A (en) | 2017-10-17 |
Family
ID=60024852
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710528798.0A Pending CN107255281A (en) | 2017-07-01 | 2017-07-01 | A kind of powder continuous heat system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107255281A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115533094A (en) * | 2022-09-30 | 2022-12-30 | 山东善香品正医药科技有限公司 | Biomedical titanium alloy heat treatment equipment and use method |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202835381U (en) * | 2012-07-05 | 2013-03-27 | 蒋华俊 | Garbage processing device |
| CN203881125U (en) * | 2014-05-29 | 2014-10-15 | 深圳市国创新能源研究院 | Expandable-material heat treatment device |
| CN204874385U (en) * | 2015-08-17 | 2015-12-16 | 湖州宜可欧环保科技有限公司 | Rotation type retort |
| 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 |
| CN106006627A (en) * | 2016-07-08 | 2016-10-12 | 张麟德 | High-temperature reaction device and graphene material production system |
| CN106318408A (en) * | 2016-11-03 | 2017-01-11 | 华北理工大学 | Screw propulsion type biomass continuous charring integrated furnace |
| CN205973807U (en) * | 2016-07-08 | 2017-02-22 | 深圳粤网节能技术服务有限公司 | Pyroreaction device and graphene materials production system |
| CN106801875A (en) * | 2017-01-13 | 2017-06-06 | 安徽未名鼎和环保有限公司 | A kind of recyclegas combustion-supporting type refuse disposal system |
| CN207081007U (en) * | 2017-07-01 | 2018-03-09 | 南京理工大学 | A kind of powder continuous heat system |
-
2017
- 2017-07-01 CN CN201710528798.0A patent/CN107255281A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202835381U (en) * | 2012-07-05 | 2013-03-27 | 蒋华俊 | Garbage processing device |
| CN203881125U (en) * | 2014-05-29 | 2014-10-15 | 深圳市国创新能源研究院 | Expandable-material heat treatment device |
| CN204874385U (en) * | 2015-08-17 | 2015-12-16 | 湖州宜可欧环保科技有限公司 | Rotation type retort |
| 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 |
| CN106006627A (en) * | 2016-07-08 | 2016-10-12 | 张麟德 | High-temperature reaction device and graphene material production system |
| CN205973807U (en) * | 2016-07-08 | 2017-02-22 | 深圳粤网节能技术服务有限公司 | Pyroreaction device and graphene materials production system |
| CN106318408A (en) * | 2016-11-03 | 2017-01-11 | 华北理工大学 | Screw propulsion type biomass continuous charring integrated furnace |
| CN106801875A (en) * | 2017-01-13 | 2017-06-06 | 安徽未名鼎和环保有限公司 | A kind of recyclegas combustion-supporting type refuse disposal system |
| CN207081007U (en) * | 2017-07-01 | 2018-03-09 | 南京理工大学 | A kind of powder continuous heat system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115533094A (en) * | 2022-09-30 | 2022-12-30 | 山东善香品正医药科技有限公司 | Biomedical titanium alloy heat treatment equipment and use method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109237490B (en) | Gasification plasma waste treatment system | |
| CN207081007U (en) | A kind of powder continuous heat system | |
| CN107075382A (en) | Waste reduction and disposal equipment | |
| CN109681886B (en) | Vertical rotary pyrolysis gasifier | |
| CN108455607A (en) | A kind of activated carbon production system of charcoal activation integral | |
| CN113102446A (en) | Pyrolysis furnace and pyrolysis system for treating waste incineration fly ash dioxin | |
| RU122465U1 (en) | AUTOMATED SOLID FUEL BOILER | |
| CN107255281A (en) | A kind of powder continuous heat system | |
| CN112694915B (en) | Wet ash discharging fixed bed gasification furnace and gasification method of organic solid waste double-layer furnace body | |
| CN106082571A (en) | Low heat value mud three change processes technique and device | |
| CN105883816B (en) | A kind of device producing nano silicon dioxide using rice husk deep oxidation | |
| CN205893035U (en) | Low heat value mud " three change " processing apparatus | |
| CN101284715A (en) | Device for baking lightweight aggregate for building materials by domestic garbage in cities and towns | |
| CN108225024B (en) | Rotary experiment furnace for continuous waste treatment | |
| CN110939934A (en) | Industrial waste treatment device for environmental protection | |
| CN112625754B (en) | Sleeve type gas-guide wet ash-discharging fixed bed gasification furnace for organic solid waste and gasification method | |
| CN110160062B (en) | Chemical waste incinerator convenient to abundant burning | |
| CN112646605B (en) | Double-layer furnace body fixed bed gasification furnace and organic solid waste gasification method | |
| CN109237492B (en) | Ash conveying mechanism and gasification plasma waste melting furnace | |
| CN110107883A (en) | Combustion system for biomass solid combustion gas cracking | |
| CN112696686A (en) | Organic solid waste gasification incineration system and method | |
| CN101576252A (en) | Gas stove with built-in combustion moving bed | |
| CN107883380A (en) | Gasification and melting refuse disposal installation and its process | |
| CN109959012A (en) | A kind of drum-type biomass and garbage pyrolysis gasification incinerator | |
| RU82214U1 (en) | CASSETTE PYROLYSIS INSTALLATION FOR COAL |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20171017 |