CN110171821A - A kind of graphitizing furnace high-temperature material cooling conveying system - Google Patents
A kind of graphitizing furnace high-temperature material cooling conveying system Download PDFInfo
- Publication number
- CN110171821A CN110171821A CN201910170531.8A CN201910170531A CN110171821A CN 110171821 A CN110171821 A CN 110171821A CN 201910170531 A CN201910170531 A CN 201910170531A CN 110171821 A CN110171821 A CN 110171821A
- Authority
- CN
- China
- Prior art keywords
- feed bin
- temperature material
- cooling
- graphitizing furnace
- conveying system
- 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
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/20—Graphite
- C01B32/205—Preparation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Tunnel Furnaces (AREA)
Abstract
The present invention relates to graphite production equipment technologies, specifically disclose a kind of graphitizing furnace high-temperature material cooling conveying system, including high temperature feed bin, the high temperature feed bin is connected to by the way that the elephant trunk of its bottom is arranged in the feed inlet of roller cooler, roller cooler cools down high-temperature material by cooling water indirectly, the discharge port of roller cooler is connected by the input terminal of the first conveyer and bucket elevator, the output end of bucket elevator is equipped with screening plant, screening plant is connect with second conveyor, the output end of second conveyor is connected to recycling feed bin, reclaimed materials the top of the warehouse is provided with bag filter.The present invention is by being arranged roller cooler in high temperature feed bin lower end, the first conveyer or bucket elevator is arranged in roller cooler downstream, solve the problems, such as that the cooling efficiency of high-temperature material cooling means in existing graphitizing furnace is low and easy waste great lot of water resources, it is simple and practical, safety and reliability is high, energy conservation and environmental protection.
Description
Technical field
The present invention relates to graphite production equipment technology, the cooling delivery system of specifically a kind of graphitizing furnace high-temperature material
System.
Background technique
With the continuous improvement of smelting technique, the demand of large-size graphite electrode is also being continuously increased currently on the market.
Graphitizing furnace is as a kind of equipment for high-temperature process such as graphite powder purifications, since high production efficiency, energy saving etc. are excellent
Point is used widely in graphite production field.
Wherein, acheson furnace (Acheson furnace) refers to the one of the naming of inventor Acheson
Kind graphitizing furnace, this is a kind of heat-treatment furnace for making the prosperity of carbide graphite crystallization, and filler coke is filled around carbide,
The resistance heating being powered indirectly using filling coke, finally makes heating object itself also generate resistance heating.Every Acheson's type
The charge weight of graphitizing furnace carbide is about 10-100 tons, in the galley body of refractory brick that carbide is vertical or horizontal
Side by side, it around is full of filler coke (being commonly called as resistance material), in its periphery again with coke powder, carbon black, silica sand/coke carbon/carbon/silicon carbide mixing
The waddings such as object carry out heat shielding with heat-insulated (being commonly called as insulation material), filler coke are full of around carbide, STRENGTH ON COKE is in furnace body
Length direction energization is warming up to 3000 DEG C or so.
Graphitizing furnace especially acheson furnace will make a large amount of high-temperature material (resistance material and guarantor in process of production
Temperature material) it is cooling.There are two types of the existing type of cooling is usual, one is natural cooling, another kind is monotubular spray.Wherein, natural
Cooling is that high-temperature material is slowly cooled down by way of air natural heat dissipation, and cooling efficiency is low；Monotubular spray is to tilt cylinder
Arrangement (conventional 3 ° or so), cylinder body outer wall spraying cooling water, cylinder rotates under motor driven, high-temperature material tilts in cylinder,
From feed end to discharging end movement under the action of rotation, at the same achieve the purpose that under the action of spraying cooling water outside cylinder it is cooling,
Although such type of cooling is more high-efficient than natural cooling, a large amount of water resource is wasted.Therefore, a kind of graphitization is designed
Furnace high-temperature material cooling conveying system, the problem of becoming current urgent need to resolve.
Summary of the invention
The purpose of the present invention is to provide a kind of graphitizing furnace high-temperature material cooling conveying systems, to solve above-mentioned background skill
The cooling efficiency of high-temperature material cooling means is low in the existing graphitizing furnace proposed in art and easy waste great lot of water resources is asked
Topic.
To achieve the above object, the invention provides the following technical scheme:
A kind of graphitizing furnace high-temperature material cooling conveying system, including the high temperature for high-temperature material in transfer graphitizing furnace
Feed bin, high temperature feed bin lower end are equipped with the bracket for being used to support high temperature feed bin, and the high temperature feed bin is by being arranged in its bottom
Elephant trunk be connected to the feed inlet of the roller cooler cooling for material, roller cooler pass through cooling water to high-temperature material into
In the ranks connect cooling, and the return water access cooling tower or waste heat boiler of the cooling water, the discharge port of roller cooler passes through the
The connection of the input terminal of one conveyer and bucket elevator, the output end of bucket elevator are equipped with the sieve for being sieved to material
Separating device, screening plant are provided at least two outlets, and the outlet be arranged in below screening plant corresponding second
Conveyer connection, the output end of second conveyor with for store it is cooling after the recycling feed bin of material be connected to, recycling feed bin lower end
It is provided with jumbo bag, reclaimed materials the top of the warehouse is provided with the bag filter for gas in Recovery Purifying feed bin；In high temperature feed bin
High-temperature material is cooled down by entering in roller cooler, by the way that the return water of cooling water is accessed cooling tower or waste heat boiler
Energy waste is avoided, meanwhile, by always with cooling water indirect heat exchange, being conducive to the activity for keeping furnace charge, being convenient for furnace charge
The comprehensive utilization of furnace charge sieves furnace charge after cooling by screening plant, the furnace charge of different-grain diameter after screening
It is delivered in corresponding recycling feed bin respectively by corresponding second conveyor, recycles the furnace charge in feed bin by being arranged at its bottom
The expects pipe in portion, which enters, carries out pack processing in jumbo bag.
As a further solution of the present invention: first conveyer is that belt feeder conveyer, drag conveyor, chain bucket are defeated
Send one of machine or screw conveyor or several combinations.
As further scheme of the invention: the screening plant is one in vibrating screen, rotary screen or roller picker
Kind or several combinations.
As further scheme of the invention: the second conveyor uses screw conveyor.
As further scheme of the invention: the roller cooler is one in membranous wall formula, jacket type or multitube
Kind or several combinations.
As further scheme of the invention: the high temperature feed bin is using circle storehouse or square storehouse；The recycling feed bin is adopted
With circle storehouse or square storehouse.
Compared with prior art, the beneficial effects of the present invention are:
1, for the present invention by the way that roller cooler is arranged in high temperature feed bin lower end, the first conveyer is arranged in roller cooler downstream
Or bucket elevator, the cooling efficiency for solving high-temperature material cooling means in existing graphitizing furnace are low and easy waste is a large amount of
The problem of water resource.
2, the present invention can be used for the cooling and conveying of acheson furnace high-temperature material, simple and practical, safety and can
By property height, good cooling results, energy conservation and environmental protection.
3, compared with conventional process mode, present invention saves a large amount of water resources, can also be abundant by the heat of furnace charge
It absorbs, has saved the energy；Furnace charge in the course of work of the present invention maintains the activity of furnace charge always with cooling water indirect heat exchange,
Be conducive to comprehensively utilize furnace charge；The present invention is provided with bag filter, reduces in system work process to environment
Pollution；Compared with traditional monotubular spray mode, by the present invention in that with roller cooler substitution monotubular spray, heat exchange efficiency
It significantly increases, is conducive to meet live actual motion requirement.
Detailed description of the invention
It to describe the technical solutions in the embodiments of the present invention more clearly, below will be to embodiment or description of the prior art
Needed in attached drawing be briefly described, it should be apparent that, the accompanying drawings in the following description is only of the invention some
Embodiment.
Fig. 1 is the structural schematic diagram of graphitizing furnace high-temperature material cooling conveying system of the present invention.
Fig. 2 is the company in graphitizing furnace high-temperature material cooling conveying system of the present invention between screening plant and second conveyor
Connect relation schematic diagram.
Company of the Fig. 3 between graphitizing furnace high-temperature material cooling conveying system high temperature feed bin of the present invention and roller cooler
Connect relation schematic diagram.
In figure: 1- high temperature feed bin, 2- roller cooler, the first conveyer of 3-, 4- bucket elevator, 5- screening plant, 6-
Second conveyor, 7- bag filter, 8- recycle feed bin, 9- jumbo bag.
Specific embodiment
In order to which technical problems, technical solutions and advantages to be solved are more clearly understood, tie below
Accompanying drawings and embodiments are closed, the present invention will be described in further detail.It should be appreciated that specific embodiment described herein is only
To explain the present invention, it is not intended to limit the present invention.
Please refer to Fig. 1-3, in one embodiment provided by the invention, a kind of cooling delivery system of graphitizing furnace high-temperature material
System, including the high temperature feed bin 1 for high-temperature material (i.e. resistance material and insulation material) in transfer graphitizing furnace (not shown), institute
It states 1 lower end of high temperature feed bin and is equipped with the bracket for being used to support high temperature feed bin 1.
It is understood that the high temperature feed bin 1 is the transfer storage device of high-temperature material, can store in graphitizing furnace
Resistance material and insulation material because charge-temperature is high, the warehouse of the high temperature feed bin 1 need to be prepared using heat-resisting material, can be with
Using heat-resistance stainless steel material, carbon steel material inner lining refractory can also be used, is specifically not construed as limiting, it can be according to practical need
It is selected.
Further, in embodiments of the present invention, the high temperature feed bin 1 passes through the elephant trunk that its bottom is arranged in and for object
Expect the feed inlet connection of cooling roller cooler 2, and then can make high-temperature material (high-temp. furnace material) in high temperature feed bin 1 can be with
It can smoothly enter into and cooled down in roller cooler 2.
Further, in embodiments of the present invention, the roller cooler 2 passes through cooling water with heat exchange form to high temperature
Material is cooled down indirectly, and the return water access cooling tower or waste heat boiler of the cooling water, by by the return water of cooling water
Cooling tower or waste heat boiler are accessed to avoid energy waste.
Specifically, by suction overhead traveling crane (not shown) or grab bucket (not shown) by graphitizing furnace (in figure not
Show) in high-temp. furnace material unload to high temperature feed bin 1, height of the charge-temperature about in 1000 DEG C or so, high temperature feed bin 1 at this time
Warm furnace charge is entered in roller cooler 2 by the elephant trunk of its bottom, and by high-temp. furnace material from the feed inlet of roller cooler 2 to going out
Material mouth conveying, roller cooler 2 cools down high-temp. furnace material in the form of heat exchange cooling water indirectly, by by furnace charge
Always with cooling water indirect heat exchange, be conducive to the activity for keeping furnace charge, convenient for the comprehensive utilization of furnace charge.
It is understood that the elephant trunk is the prior art, it is generally used for the blanking cloth of powdery, graininess, block material
Material is installed below the bottom or conveying device blanking port of blanking bin more, is blanking bin or conveying device and material main equipment
Between conveying bridge.
Further, in embodiments of the present invention, the discharge port of the roller cooler 2 passes through the first conveyer 3 and bucket
The input terminal of formula elevator 4 connects, and furnace charge carries out defeated in the first conveyer 3 through supercooling heel row to 2 downstream of roller cooler
It send, 3 discharge port of the first conveyer connects bucket elevator 4, and furnace charge enters bucket elevator 4 by the first conveyer 3, mentioned by bucket type
The height space that machine 4 is promoted is risen to arrange screening plant 5, second conveyor 6, bag filter 7, recycling feed bin 8 and jumbo bag 9.
In another embodiment provided by the invention, the output end (being arranged at top) of the bucket elevator 4 is equipped with
Screening plant 5 for being sieved to material, the screening plant 5 are provided at least two outlets, and the outlet and set
It sets the corresponding second conveyor 6 below the screening plant 5 to connect, by setting at least two for the screening plant 5
A outlet, and the outlet is connected with the corresponding second conveyor 6 being arranged in below the screening plant 5, and then can be led to
It crosses screening plant 5 while screening out varigrained material, effectively increase screening efficiency.
Further, in embodiments of the present invention, the output end of the second conveyor 6 with for store it is cooling after material
Recycling feed bin 8 be connected to, 8 lower end of recycling feed bin is provided with jumbo bag 9, by screening plant 5 to furnace charge after cooling progress
The furnace charge of screening, different-grain diameter after screening is delivered to corresponding recycling feed bin 8 by corresponding second conveyor 6 respectively
It is interior, it recycles the furnace charge in feed bin 8 and passes through and the expects pipe of its bottom is set enters and carry out pack processing in jumbo bag 9.
Further, in embodiments of the present invention, it is provided at the top of the recycling feed bin 8 in Recovery Purifying feed bin 8
The bag filter 7 of gas continuously, absolutely handles all gases for entering recycling feed bin 8 by bag filter 7
(including the air containing dust), gas is direct after dust and pernicious gas are removed after being purified by bag filter 7 and will be purified
It is discharged into atmosphere, avoids and pollutes the environment.
It should be noted that valve is equipped between above equipment and equipment, i.e., the described high temperature feed bin 1, roller cooler
2, the first conveyer 3, bucket elevator 4, screening plant 5, second conveyor 6, bag filter 7, recycling feed bin 8 and jumbo bag
It is equipped with valve at 9 interconnection, so that valve can be closed when emergency, or is examined convenient for independent off-the-line equipment
The work such as repair.
Before system work, the roller cooler 2 need to be passed through cooling water, in actual use, use softened water as far as possible, because
For the easy fouling of industrial water, and fouling will affect the cooling effect of roller cooler 2, must such as use industrial water, then need
Setting leaving water temperature is generally no greater than 50 DEG C, and needs timely scale removal.
It should be noted that the return water of the cooling water can access cooling tower (not shown), it is again introduced into after cooling
It is carried out in roller cooler 2 using recycling for cooling water may be implemented, avoid waste.
Further, if waste heat boiler is had in factory, the cooling water after heating can be subjected to heat by waste heat boiler
The heat of amount recycling, such high-temp. furnace material release can be used effectively, and then reduce energy waste.
When system works, graphitizing furnace (is schemed by suction overhead traveling crane (not shown) or grab bucket (not shown)
In be not shown) in high-temp. furnace material (resistance material and insulation material) unload to high temperature feed bin 1, charge-temperature is about at 1000 DEG C at this time
Or so, the high-temp. furnace material in high temperature feed bin 1 is entered in roller cooler 2 by the elephant trunk of orlop, and roller cooler 2 passes through cooling
Water cools down high-temp. furnace material in the form of heat exchange, and furnace charge first through supercooling heel row to 2 downstream of roller cooler is defeated
It send in machine 3, furnace charge is delivered into bucket elevator 4 by the first conveyer 3, and furnace charge enters after the promotion of bucket elevator 4
It is arranged in the screening plant 5 of 8 top of recycling feed bin, the varigrained material after the screened screening of device 5 by exporting accordingly
The second conveyor 6 for escaping and enter downstream is delivered in corresponding recycling feed bin 8 through second conveyor 6, recycles in feed bin 8
Furnace charge entered by the expects pipe of orlop and carry out pack processing in jumbo bag 9, jumbo bag 9 is finally transported to warehouse.
It is understood that by the temperature of charge general control after cooling of roller cooler 2 at 80 DEG C or less (mainly
In view of the heat resistance of the subsequent jumbo bag 9 used), cold in-water temperature is generally located on 30 DEG C or so, return water temperature and
Drop temperature is close, and general control is at 80 DEG C hereinafter, can also be avoided by the way that return water is accessed cooling tower or waste heat boiler
Energy waste.
In another embodiment provided by the invention, first conveyer 3 is belt feeder conveyer, scraper plate conveying
One of machine, bucket chain conveyor or screw conveyor or several combinations, are specifically not construed as limiting, but preferably belt feeder conveying
Machine, certainly, above-mentioned only preferred embodiment can specifically set according to actual needs, here and be not construed as limiting.
Further, in embodiments of the present invention, the screening plant 5 is in vibrating screen, rotary screen or roller picker
One or several kinds combination, is specifically not construed as limiting, but preferred vibrating screen, the screen size of the screening plant 5 is wanted according to user
It asks and is selected, certainly, above-mentioned only preferred embodiment, the screening plant 5 can also be such as equal thick screen, probability equal thick screen, relax
Other screening plants such as sieve or shaker screen are opened, sets with specific reference to actual demand, here and is not construed as limiting.
Further, in embodiments of the present invention, because conveying distance is short, spiral shell is usually used in the second conveyor 6
Revolve conveyer.
Further, in embodiments of the present invention, the roller cooler 2 is in membranous wall formula, jacket type or multitube
One or several kinds combination, be specifically not construed as limiting, according to graphitizing furnace it is different go out grain requirement, can be used membranous wall formula, jacket type,
The forms such as multitube here and are not construed as limiting.
Further, in embodiments of the present invention, the high temperature feed bin 1 is using circle storehouse or square storehouse.
Further, in embodiments of the present invention, the recycling feed bin 8 is using circle storehouse or square storehouse.
It should be noted that the graphitizing furnace high-temperature material cooling conveying system is furnished with full-automatic control system and equipment
Failure warning system, it is safe and reliable to operation, unattended fully automatic operation may be implemented, by remotely controlling, greatly reduce
Cost of labor.
It will be understood by those skilled in the art that structure shown in Fig. 1-3, only with application scheme relevant portion
Structural schematic diagram does not constitute the restriction of the graphitizing furnace high-temperature material cooling conveying system described in application scheme, specifically
Graphitizing furnace high-temperature material cooling conveying system may include than more or fewer equipment as shown in the figure, or combination is certain sets
It is standby, or arranged with different equipment, it is not directed to part in the system and is the same as those in the prior art or can be used the prior art
It is realized.
For example, in above-described embodiment, first conveyer 3 is because the reasons such as place limitation can also be not provided with, directly
It connects and the roller cooler 2 connects with bucket elevator 4；The second conveyor 6 of 5 lower end of the screening plant setting is only one
Kind engineering construction example can export screening plant 5 by slipping if the outlet of screening plant 5 is enough at a distance from recycling feed bin 8
Pipe directly connects with recycling feed bin 8；If not sieving requirement, the screening plant 5 and second conveyor 6 can also be not provided with,
Directly the bucket elevator 4 outlet is connected by elephant trunk with recycling feed bin 8.
The beneficial effects of the present invention are: graphitizing furnace high-temperature material cooling conveying system of the present invention passes through in high temperature feed bin 1
Roller cooler 2 is arranged in lower end, and the first conveyer 3 or bucket elevator 4 is arranged in 2 downstream of roller cooler, and system end is set
Put back into receiving warehouse 8 and store material, solve high-temperature material cooling means in existing graphitizing furnace cooling efficiency is low and Yi Lang
The problem of taking great lot of water resources；The present invention can be used for the cooling and conveying of acheson furnace high-temperature material, and the system is easy
Practical, Automatic Control, safety and reliability is high, and good cooling results, energy conservation and environmental protection preferably solves current graphitizing furnace
High-temperature material processing system there are the problem of, can be used for new construction, also can be used as original system transformation use；With conventional process side
Formula compares, and present invention saves a large amount of water resources, can also fully absorb the heat of furnace charge, improve the heat of waste heat boiler
Efficiency has saved the energy；Furnace charge in the course of work of the present invention maintains the activity of furnace charge always with cooling water indirect heat exchange,
Be conducive to the comprehensive utilization of furnace charge；The present invention is provided with bag filter, will not generate fugitive dust in system work process, avoid
Pollution environment, meets the requirement carried out production strictly in line with rules and regulations；Compared with traditional monotubular spray mode, by the present invention in that cold with roller
But machine 2 substitutes monotubular spray, and heat exchange efficiency significantly increases, is conducive to meet live actual motion requirement.
The equipment occurred in this article can be electrically connected with extraneous main controller and 220V alternating current, and main controller can be calculating
Machine etc. plays the conventionally known equipment of control.
In the description of the present invention unless specifically defined or limited otherwise, term " installation ", " connected ", " connection " are answered
It is interpreted broadly, for example, it may be being fixedly connected, may be a detachable connection, or be integrally connected；It can be mechanical connect
It connects, is also possible to be electrically connected；It can be directly connected, can also can be in two elements indirectly connected through an intermediary
The connection in portion.For the ordinary skill in the art, the tool of above-mentioned term in the present invention can be understood with concrete condition
Body meaning.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all in essence of the invention
Made any modifications, equivalent replacements, and improvements etc., should all be included in the protection scope of the present invention within mind and principle.
Claims (7)
1. a kind of graphitizing furnace high-temperature material cooling conveying system, including the high temperature material for high-temperature material in transfer graphitizing furnace
Storehouse (1), high temperature feed bin (1) lower end are equipped with the bracket for being used to support high temperature feed bin (1), which is characterized in that the high temperature material
The feed inlet that storehouse (1) passes through the elephant trunk that its bottom the is arranged in roller cooler (2) cooling with material is used for is connected to；
The roller cooler (2) cools down high-temperature material by cooling water indirectly, and the return water access of the cooling water
Cooling tower or waste heat boiler；
The discharge port of the roller cooler (2) is connect by the first conveyer (3) with the input terminal of bucket elevator (4), institute
The output end of bucket elevator (4) is stated equipped with the screening plant (5) for being sieved to material, the screening plant (5) sets
At least two outlets are equipped with, and the outlet connects with the corresponding second conveyor (6) being arranged below the screening plant (5)
It connects；
The output end of the second conveyor (6) is connected to recycling feed bin (8), and recycling feed bin (8) lower end is provided with jumbo bag
(9), the bag filter (7) for Recovery Purifying feed bin (8) interior gas is provided at the top of recycling feed bin (8).
2. graphitizing furnace high-temperature material cooling conveying system according to claim 1, which is characterized in that first conveying
Machine (3) is one of belt feeder conveyer, drag conveyor, bucket chain conveyor or screw conveyor or several combinations.
3. graphitizing furnace high-temperature material cooling conveying system according to claim 1, which is characterized in that the screening plant
It (5) is one of vibrating screen, rotary screen or roller picker or several combinations.
4. graphitizing furnace high-temperature material cooling conveying system according to claim 3, which is characterized in that second conveying
Machine (6) uses screw conveyor.
5. graphitizing furnace high-temperature material cooling conveying system according to claim 4, which is characterized in that the roller is cooling
Machine (2) is one of membranous wall formula, jacket type or multitube or several combinations.
6. -5 any graphitizing furnace high-temperature material cooling conveying system according to claim 1, which is characterized in that the height
Warm feed bin (1) is using circle storehouse or square storehouse.
7. -5 any graphitizing furnace high-temperature material cooling conveying system according to claim 1, which is characterized in that described time
Receiving warehouse (8) is using circle storehouse or square storehouse.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910170531.8A CN110171821A (en) | 2019-03-07 | 2019-03-07 | A kind of graphitizing furnace high-temperature material cooling conveying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910170531.8A CN110171821A (en) | 2019-03-07 | 2019-03-07 | A kind of graphitizing furnace high-temperature material cooling conveying system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110171821A true CN110171821A (en) | 2019-08-27 |
Family
ID=67689144
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910170531.8A Pending CN110171821A (en) | 2019-03-07 | 2019-03-07 | A kind of graphitizing furnace high-temperature material cooling conveying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110171821A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111471828A (en) * | 2020-04-29 | 2020-07-31 | 浙江神风风电科技有限公司 | Full-automatic carburant production line |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102963889A (en) * | 2012-12-06 | 2013-03-13 | 中钢集团新型材料（浙江）有限公司 | Efficiently environment-friendly graphitization furnace cooling technology |
| CN202962841U (en) * | 2012-12-06 | 2013-06-05 | 中钢集团新型材料（浙江）有限公司 | Multifunctional screening system of traveling crane |
| WO2014194563A1 (en) * | 2013-06-04 | 2014-12-11 | 四川玖长科技有限公司 | Improved method for mass production of phosphoric acid with rotary kiln |
-
2019
- 2019-03-07 CN CN201910170531.8A patent/CN110171821A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102963889A (en) * | 2012-12-06 | 2013-03-13 | 中钢集团新型材料（浙江）有限公司 | Efficiently environment-friendly graphitization furnace cooling technology |
| CN202962841U (en) * | 2012-12-06 | 2013-06-05 | 中钢集团新型材料（浙江）有限公司 | Multifunctional screening system of traveling crane |
| WO2014194563A1 (en) * | 2013-06-04 | 2014-12-11 | 四川玖长科技有限公司 | Improved method for mass production of phosphoric acid with rotary kiln |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111471828A (en) * | 2020-04-29 | 2020-07-31 | 浙江神风风电科技有限公司 | Full-automatic carburant production line |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| WO2019161639A1 (en) | Dry type centrifugal granulation and waste heat recycling and utilization system for liquid molten slag | |
| CN108330235B (en) | Liquid slag granulation and waste heat recovery device | |
| CN105036168B (en) | High-temperature-calcined [alpha]-Al2O3 production energy-saving apparatus and novel method | |
| CN106564900A (en) | Clean, efficient and safe process for preparing calcium carbide powder through molten-state calcium carbide cooling | |
| CN107523686B (en) | A kind of device and method preparing Iron concentrate for red mud suspension roasting | |
| CN101749947B (en) | Petroleum coke calcining process and equipment for large-capacity pot-type calcining furnace | |
| CN107091569A (en) | Rotary kiln and the polygenerations systeme that metal hydride is produced using the rotary kiln | |
| CN211012481U (en) | Vertical preheater | |
| CN115678582A (en) | Horizontal wind power blade recovery reaction device and wind power blade recovery method | |
| CN110171821A (en) | A kind of graphitizing furnace high-temperature material cooling conveying system | |
| CN210065182U (en) | High-temperature material cooling and conveying system of graphitizing furnace | |
| CN102491329A (en) | Thermal feeding method and device for calcium carbide furnace | |
| CN205472690U (en) | Special feed bin device that adds of carbon disulfide gasification reaction stove | |
| CN216725853U (en) | Production device for preparing arsenic trioxide from crude arsenic | |
| CN217541454U (en) | Lithium cell cathode material miropowder system of calcining in succession | |
| CN217438227U (en) | Horizontal vibration type hot direct reduced iron conveying device | |
| CN110631378A (en) | Vertical preheater | |
| CN202246809U (en) | Treatment and recycling device of waste residue after metal magnesium smelting | |
| CN109163569B (en) | Division vertical type sinter cooler and sinter cooling method | |
| CN206529069U (en) | A kind of New water jacket cools down dilute phase pneumatic conveying system | |
| CN110514019B (en) | High-temperature powdery material cooling process and device | |
| CN214371676U (en) | Automatic kiln equipment for producing kaolin | |
| CN207775323U (en) | A kind of Novel electric furnace zinc powder production line | |
| CN202083233U (en) | Inner tube for preheater of rotary cement kiln | |
| CN210085290U (en) | Device for granulating molten smelting slag glass and recovering waste heat |
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 |