CN104724690A - Carbon anode pot calciner automatic continuous batching apparatus - Google Patents
Carbon anode pot calciner automatic continuous batching apparatus Download PDFInfo
- Publication number
- CN104724690A CN104724690A CN201310711858.4A CN201310711858A CN104724690A CN 104724690 A CN104724690 A CN 104724690A CN 201310711858 A CN201310711858 A CN 201310711858A CN 104724690 A CN104724690 A CN 104724690A
- Authority
- CN
- China
- Prior art keywords
- batching
- calcine furnace
- type calcine
- rubber conveyer
- automatic continuous
- 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.)
- Granted
Links
Abstract
The invention discloses a carbon anode pot calciner automatic continuous batching apparatus. According to the carbon anode pot calciner automatic continuous batching apparatus, automatic continuous batching is realized successively via a pot calciner (4), a pot calciner discharging rubber belt conveyor (5), a first bucket elevator (6), an electric hydraulic three-way distributor (7), a back batching material bin (8), an electric hydraulic bulkhead gate (9), an electro-vibrating feeder (10), a rubber belt constant weight feeder (11), a second bucket elevator (12), and a mixed rubber belt conveyer (2). According to the carbon anode pot calciner automatic continuous batching apparatus, a green petroleum coke batching method and a green petroleum coke back-batching calcined material batching method can be adopted based on volatile matter content of green petroleum coke. The carbon anode pot calciner automatic continuous batching apparatus is capable of realizing uniform batching; calcined material product quality is stable; back batching is capable of realizing quantitative batching; volatile matter content inside furnace is controlled strictly; furnace thermal condition is stable; operation maintenance of the pot calciner is reduced; back batching material utilization ratio is increased; circulation quantity is reduced; pot calciner energy production is increased; and production area sanitary conditions are improved.
Description
Technical field
The present invention relates to a kind of dosing unit, in particular for the automatization continous batching device of carbon anode can-type calcine furnace.
Background technology
Calcining is the operation to quality product important during aluminum carbon anode is produced, and calcination process directly has influence on quality product and the economic benefit of carbon anode enterprise.The major equipment of calcining has can-type calcine furnace and rotary kiln.Go up in the prices of raw and semifnished materials, quality is unstable, and under development trend in short supply, the unique carbon burnt loss of can-type calcine furnace is low, good product quality, and sulfur dioxide emissions are few, and UTILIZATION OF VESIDUAL HEAT IN is worth high numerous advantage, obtains the widespread use of aluminum i ndustry.Because the quality fluctuation of refinery coke raw material is large, causes the coking of can-type calcine furnace burner hearth in order to avoid volatile content is too high, need aborning to consider back to join after-smithing petroleum coke, enter stove with raw petroleum coke mixture, to reduce volatile content in burner hearth.In traditional processing technology, back ingredient will transport raw petroleum coke workshop back by automobile, then grabs into receiving hopper by bridge grabbing crane, allocates material before calcined delivery system into.And along with the quality fluctuation of raw material large, increasing enterprise adopts petroleum coke homogenizing scheme to improve the quality fluctuation of raw material, district is stored up due to back ingredient cannot be arranged in petroleum coke homogenizing storehouse, this becomes loaded down with trivial details with regard to the technique making back ingredient and come back to material before calcined delivery system, needs to increase back ingredient warehouse again, back ingredient material loading and feed system, increase investment, can not automatization continous batching, there is automobile discharging in back ingredient region, environment and sanitary condition poor.
Summary of the invention
The technical problem to be solved in the present invention is: provide a kind of carbon anode can-type calcine furnace automatization continous batching device, solve can-type calcine furnace and can not realize automatization continous batching, and back ingredient to come back to the technical process of material before calcined delivery system loaded down with trivial details, can not work continuously, transloading equipment is many, shipment distance is long, there is secondary storage, returns the problem of joining regional environment and sanitary condition difference.
Technical scheme of the present invention is: by back ingredient by continuous conveying equipment and the raw petroleum coke mixture come from petroleum coke homogenizing storehouse, realize automated operation and continuous seepage operation, reduce back ingredient intermediate storage.The concrete plan of establishment of device is as follows:
It is can-type calcine furnace discharge rubber conveyer below can-type calcine furnace, the end of can-type calcine furnace discharge rubber conveyer is the first chapelet, first chapelet discharge port is connected with electro hydraulic actuating tee joint distributor, electro hydraulic actuating tee joint distributor exit end respectively with back ingredient storehouse with forge rear material storing and transporting system rubber conveyer and be communicated with, bottom, back ingredient storehouse is that electricity surges bulkhgead gate, it is electro-vibrating feeder that electricity surges below bulkhgead gate, electro-vibrating feeder discharge end has rubber belt quantitative feeding machine, rubber belt quantitative feeding machine end is the second chapelet, second chapelet discharge port is communicated with mixture rubber conveyer, mixture rubber conveyer discharge end has material before calcined storehouse, material before calcined storehouse is connected with can-type calcine furnace, mixture rubber conveyer feed end is also communicated with petroleum coke homogenizing storehouse supplied materials rubber conveyer end.
Forge rear material to be discharged by can-type calcine furnace discharge mechanism, the first chapelet entrance is collected to through can-type calcine furnace discharge rubber conveyer, be promoted to after certain altitude through chapelet, qualified calcined coke through electro hydraulic actuating tee joint distributor be delivered to forge after expect storing and transporting system rubber conveyer, defective material or be delivered to back ingredient storage according to the back ingredient of need of production through electro hydraulic actuating tee joint distributor and deposit, when material before calcined volatile content is too high need mixture back ingredient time, electricity at the bottom of back ingredient storehouse surge bulkhgead gate open, back ingredient by electro-vibrating feeder to rubber belt quantitative feeding machine feed, then after the second chapelet is promoted to certain altitude, be discharged into raw petroleum coke and back ingredient mixture rubber conveyer, the raw petroleum coke transported with petroleum coke homogenizing storehouse rubber conveyer is again in this mixture, feedstock transportation after mixture is suitable stores up to material before calcined warehousing, feed in can-type calcine furnace when can-type calcine furnace needs charging and calcine.
Beneficial effect of the present invention is embodied in: for raw petroleum coke and back ingredient achieve even mixture, forges rear material constant product quality; Back ingredient realizes quantitative ingredient, volatile content in strict control stove, and in stove, thermal technology state is stablized, and reduces the Operation and Maintenance of can-type calcine furnace, increases the utilization ratio of back ingredient, reduces internal circulating load, improves the production capacity of can-type calcine furnace; Can operator be reduced, reduce labour intensity; Reduce back ingredient storage and transloading equipment, reduce investment; Can realize automatically controlling, level of automation is high; Can realize production serialization, back ingredient fed distance is short, and technique is more reasonable, produces more flexible; Avoid the discharging of back ingredient automobile, improve high dust atmosphere, improve production area sanitary condition.
Accompanying drawing explanation
Fig. 1 is carbon anode can-type calcine furnace automatization continous batching apparatus structure schematic diagram.
Wherein, 1 is petroleum coke homogenizing storehouse supplied materials rubber conveyer; 2 is mixture rubber conveyer (raw petroleum coke and back ingredient); 3 is material before calcined storehouse; 4 is can-type calcine furnace; 5 is can-type calcine furnace discharge rubber conveyer; 6 is the first chapelet; 7 is electro hydraulic actuating tee joint distributor; 8 is back ingredient storehouse; 9 to surge bulkhgead gate for electricity; 10 is electro-vibrating feeder; 11 is rubber belt quantitative feeding machine; 12 is the second chapelet; 13 for forging rear material storing and transporting system rubber conveyer.
Embodiment
As shown in Figure 1, a kind of carbon anode can-type calcine furnace automatization continous batching device, comprise can-type calcine furnace 4, it is can-type calcine furnace discharge rubber conveyer 5 below can-type calcine furnace 4, the end of can-type calcine furnace discharge rubber conveyer 5 is the first chapelet 6, first chapelet 6 discharge port is connected with electro hydraulic actuating tee joint distributor 7, electro hydraulic actuating tee joint distributor 7 exit end respectively with back ingredient storehouse 8 with forge rear material storing and transporting system rubber conveyer 13 and be communicated with, bottom, back ingredient storehouse 8 is that electricity surges bulkhgead gate 9, it is electro-vibrating feeder 10 that electricity surges below bulkhgead gate 9, electro-vibrating feeder 10 discharge end has rubber belt quantitative feeding machine 11, rubber belt quantitative feeding machine 11 end is the second chapelet 12, second chapelet 12 discharge port is communicated with mixture rubber conveyer 2, mixture rubber conveyer 2 discharge end has material before calcined storehouse 3, material before calcined storehouse 3 is connected with can-type calcine furnace 4, mixture rubber conveyer 2 feed end is also communicated with petroleum coke homogenizing storehouse supplied materials rubber conveyer 1 end, connection or the connection of said apparatus adopt pneumatic elephant trunk.
When raw petroleum coke volatile content can not to cause in can-type calcine furnace calcining to produce coking, raw petroleum coke in homogenizing storehouse after homogenizing, carrys out rubber conveyer 1 by petroleum coke homogenizing storehouse and is transported to material before calcined storehouse 3 and calcines for can-type calcine furnace 4.When raw petroleum coke volatile content too high easily in can-type calcine furnace calcining produce coking, calcined coke can not normal discharge, and now will adopt back ingredient and raw petroleum coke mixture, reduction enters the volatile content of raw material in can-type calcine furnace 4.Back ingredient is the refinery coke after calcining, can-type calcine furnace 4 is by discharge mechanism discharge, qualified calcined coke is collected by can-type calcine furnace discharge rubber conveyer 5, enter the first chapelet 6 and be promoted to certain altitude, part calcined coke enters forge rear material storing and transporting system by forging rear material storing and transporting system rubber conveyer 13, another part calcined coke, as back ingredient, by electro hydraulic actuating tee joint distributor 7, enters back ingredient storehouse 8 and stores (defective calcined coke all enters back ingredient storehouse 8 and stores).When needs back ingredient mixture, the electricity at the end, back ingredient storehouse 8 bulkhgead gate 9 that surges is opened, back ingredient passes through electro-vibrating feeder 10 to rubber belt quantitative feeding machine 11 feed, rubber belt quantitative feeding machine 11 is by regulating variable-frequency motor, realize the accurate proportioning of back ingredient, then back ingredient is promoted to certain altitude through the second chapelet 12, be discharged into mixture rubber conveyer 2, thus with the raw petroleum coke transported by homogenizing storehouse in this mixture, feedstock transportation after mixture stores to can-type calcine furnace material before calcined storehouse 3, calcining in can-type calcine furnace 4 is fed when can-type calcine furnace 4 needs charging.
Claims (1)
1. a carbon anode can-type calcine furnace automatization continous batching device, comprise can-type calcine furnace (4), it is characterized in that: can-type calcine furnace (4) below is can-type calcine furnace discharge rubber conveyer (5), the end of can-type calcine furnace discharge rubber conveyer (5) is the first chapelet (6), first chapelet (6) discharge port is connected with electro hydraulic actuating tee joint distributor (7), electro hydraulic actuating tee joint distributor (7) exit end respectively with back ingredient storehouse (8) with forge rear material storing and transporting system rubber conveyer (13) and be communicated with, back ingredient storehouse (8) bottom is that electricity surges bulkhgead gate (9), electricity surges bulkhgead gate (9) below for electro-vibrating feeder (10), electro-vibrating feeder (10) discharge end has rubber belt quantitative feeding machine (11), rubber belt quantitative feeding machine (11) end is the second chapelet (12), second chapelet (12) discharge port is communicated with mixture rubber conveyer (2), mixture rubber conveyer (2) discharge end has material before calcined storehouse (3), material before calcined storehouse (3) is connected with can-type calcine furnace (4), mixture rubber conveyer (2) feed end is also communicated with petroleum coke homogenizing storehouse supplied materials rubber conveyer (1) end.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310711858.4A CN104724690B (en) | 2013-12-23 | 2013-12-23 | A kind of carbon anode can-type calcine furnace automatization continuous batching device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310711858.4A CN104724690B (en) | 2013-12-23 | 2013-12-23 | A kind of carbon anode can-type calcine furnace automatization continuous batching device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104724690A true CN104724690A (en) | 2015-06-24 |
| CN104724690B CN104724690B (en) | 2016-08-31 |
Family
ID=53449195
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310711858.4A Active CN104724690B (en) | 2013-12-23 | 2013-12-23 | A kind of carbon anode can-type calcine furnace automatization continuous batching device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104724690B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112877086A (en) * | 2021-01-25 | 2021-06-01 | 焦作钧菲津材科技有限公司 | Petroleum coke calcination control method |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101759176A (en) * | 2008-12-23 | 2010-06-30 | 贵阳铝镁设计研究院 | Method and device for collocating blending material of pot-type calciner |
| CN101759175A (en) * | 2008-12-23 | 2010-06-30 | 贵阳铝镁设计研究院 | Process and equipment for blending calcined material during calcining high volatile material by pot-type calciner |
| CN203612962U (en) * | 2013-12-23 | 2014-05-28 | 贵阳铝镁设计研究院有限公司 | Continuous batching device for pot-type calcination furnace |
-
2013
- 2013-12-23 CN CN201310711858.4A patent/CN104724690B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101759176A (en) * | 2008-12-23 | 2010-06-30 | 贵阳铝镁设计研究院 | Method and device for collocating blending material of pot-type calciner |
| CN101759175A (en) * | 2008-12-23 | 2010-06-30 | 贵阳铝镁设计研究院 | Process and equipment for blending calcined material during calcining high volatile material by pot-type calciner |
| CN203612962U (en) * | 2013-12-23 | 2014-05-28 | 贵阳铝镁设计研究院有限公司 | Continuous batching device for pot-type calcination furnace |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112877086A (en) * | 2021-01-25 | 2021-06-01 | 焦作钧菲津材科技有限公司 | Petroleum coke calcination control method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104724690B (en) | 2016-08-31 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105985036B (en) | A kind of processing method of ardealite | |
| CN108193016B (en) | Intelligent control charging device of horizontal continuous charging electric arc furnace and use method | |
| CN109880959B (en) | Method for increasing addition proportion of converter scrap steel | |
| CN204454892U (en) | A kind of phosphogypsum machining production line | |
| CN205240803U (en) | A even material loading lifting machine for tealeaves automatic production line | |
| CN210128625U (en) | Automatic feeding system of brown corundum smelting furnace | |
| CN203612962U (en) | Continuous batching device for pot-type calcination furnace | |
| CN203601932U (en) | Magnesium reduction vertical tank automatic feeding system | |
| CN104724690A (en) | Carbon anode pot calciner automatic continuous batching apparatus | |
| CN102826319B (en) | Stock yard | |
| CN203945497U (en) | A kind of castable proportioner | |
| CN204525801U (en) | Mixing station cold burden automatic charging device | |
| CN210084324U (en) | Automatic coal blending system in pit of mine | |
| CN210128624U (en) | Automatic material preparation system of brown corundum smelting furnace | |
| CN106429320A (en) | Automatic feed delivery device for medium-frequency heating stove | |
| CN104118061B (en) | A kind of castable proportioner | |
| CN107363978B (en) | Automatic feeding method for brick machine feeding bin | |
| CN103041908B (en) | Novel smashed rubber conveying system and smashed rubber conveying method using same | |
| CN103253673B (en) | Charging equipment and charging method of large-scale silicon carbide smelting furnace | |
| CN202704356U (en) | Intelligent physical distribution loading and unloading transport system | |
| CN201666811U (en) | Corrosion resistant and high temperature resistant clinker brick automatic weigh-batching system | |
| CN203333487U (en) | Cement raw material homogenization system | |
| CN101955071A (en) | System and method for delaying batching of petroleum coke before calcination | |
| CN210128623U (en) | Automatic batching system of brown corundum smelting furnace | |
| CN205167180U (en) | Go up undercarriage marshalling system suitable for quadratic code burns |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| EXSB | Decision made by sipo to initiate substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |