CN205933242U - Pot calciner temperature -adjusting control device - Google Patents
Pot calciner temperature -adjusting control device Download PDFInfo
- Publication number
- CN205933242U CN205933242U CN201620738362.5U CN201620738362U CN205933242U CN 205933242 U CN205933242 U CN 205933242U CN 201620738362 U CN201620738362 U CN 201620738362U CN 205933242 U CN205933242 U CN 205933242U
- Authority
- CN
- China
- Prior art keywords
- temperature
- calcine furnace
- type calcine
- control unit
- pot calciner
- 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.)
- Active
Links
- 238000004891 communication Methods 0.000 claims abstract description 7
- 238000007599 discharging Methods 0.000 claims description 13
- 239000000470 constituent Substances 0.000 abstract description 7
- 230000033228 biological regulation Effects 0.000 abstract description 3
- 230000005622 photoelectricity Effects 0.000 abstract 3
- 230000005611 electricity Effects 0.000 abstract 1
- 238000001354 calcination Methods 0.000 description 10
- 238000000034 method Methods 0.000 description 9
- 239000003546 flue gas Substances 0.000 description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 6
- 239000007789 gas Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 238000001514 detection method Methods 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- 239000002008 calcined petroleum coke Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000002006 petroleum coke Substances 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005242 forging Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
Landscapes
- Vertical, Hearth, Or Arc Furnaces (AREA)
Abstract
The utility model discloses a pot calciner temperature -adjusting control device, the device includes: the photoelectricity temperature sensor who installs at the pot calciner flame path installs the air conditioner at pot calciner air channel entry, installs the negative pressure regulator at pot calciner set flue outlet, and photoelectricity temperature sensor, air conditioner, negative pressure regulator are connected with the pot calciner temperature sensor 1 electricity respectively, pot calciner the control unit is connected with the remote client communication. Photoelectricity temperature sensor determine flame path real -time temperature is not when the target temperature scope, the direct send instruction of pot calciner the control unit, perhaps the send instruction of remote client elder generation gives pot calciner the control unit, give air conditioner by pot calciner the control unit send instruction again, negative pressure regulator adjusts respective degree of opening, and then fugitive constituent burning degree in the regulation flame path, automatically, transfer the scope to target temperature with flame path real -time temperature accurately, pot calciner's degree of automation has been improved.
Description
Technical field
This utility model is related to can-type calcine furnace field, more particularly, to a kind of can-type calcine furnace discharging temperature control device.
Background technology
At present, it is both needed to using stone after forging in fields such as aluminium cathode product, graphite electrode, carbon electrode, carburant, titanium smeltings
Oil coke, the calciner of petroleum coke mainly has rotary kiln and can-type calcine furnace both.Wherein, can-type calcine furnace is because of its scaling loss
Little, burning quality is high, realize the advantages of no extra fuel is calcined and be widely used in domestic carbon element factory and produce aluminum prebake
After-smithing petroleum coke needed for anode.But with respect to rotary kiln, can-type calcine furnace still suffers from following obvious defect:Can-type calcine furnace
Automaticity is low, the regulation of calcining heat and control mainly by workman experience, the temperature error of one side manual observation is relatively
Greatly it is impossible to realize the accurate regulation of temperature, and temperature is the major control factors of calcined petroleum coke primary quality measure true density,
Therefore product quality is difficult to ensure that;On the other hand, workman's energy is limited, and temperature can not adjust in time, causes calcining furnace temperature to neglect
Height is suddenly low, decreases the service life of can-type calcine furnace;3rd, the low amount of labour leading to workman of can-type calcine furnace automaticity
Greatly, cost of labor increases;4th, the high homoiothermic workman's shortage of resources of state-of-the art, the new production capacity company that puts into is difficult to find
To outstanding personnel.Therefore, the automaticity improving can-type calcine furnace is extremely urgent.
Content of the invention
In view of this, technical problem to be solved in the utility model is:A kind of can-type calcine furnace homoiothermic is provided to control dress
Put, improve automatization's homoiothermic degree of can-type calcine furnace it is ensured that product quality, reduce cost of labor.
For solving above-mentioned technical problem, the technical solution of the utility model is:Can-type calcine furnace discharging temperature control device, bag
Include:
Photoelectric temperature sensor, described photoelectric temperature sensor is arranged on the quirk of can-type calcine furnace;
Air conditioner, described air conditioner is arranged on the air channel entrance of described can-type calcine furnace;
Draft regulator, described draft regulator is arranged on the collection flue outlet of described can-type calcine furnace;
Described photoelectric temperature sensor, described air conditioner, described draft regulator respectively with described can-type calcine furnace
Control unit electrical connection.
Further, the control unit of described can-type calcine furnace is also connected with remote client's end communication.
Based on same inventive concept, this utility model also provides a kind of homoiothermic of can-type calcine furnace discharging temperature control device to control
Method.
The homoiothermic control method of described can-type calcine furnace discharging temperature control device comprises the following steps:
Set quirk target temperature as T0;
Photoelectric temperature sensor detection quirk real time temperature is T1, and real time temperature signal is sent to can-type calcine furnace
Control unit;
Real time temperature and target temperature are compared and judge and send instruction by the control unit of can-type calcine furnace:
If T1 is > T0, send instructions to air conditioner, reduce the open degree of air conditioner, reduce air inlet amount;
Selectively, send instructions to draft regulator, the open degree of intensified negative pressure actuator, increase flue gas gas output;
If T1 is < T0, send instructions to air conditioner, the open degree of increase air actuator, increase air air inflow;
Selectively, send instructions to draft regulator, reduce the open degree of draft regulator, reduce flue gas gas output.
Further, the control unit of described can-type calcine furnace is connected with remote client's end communication, described homoiothermic controlling party
Method is further comprising the steps of:Real time temperature and target temperature are compared after judgement by the control unit of can-type calcine furnace, will sentence
Disconnected result transmits Terminal Server Client, and Terminal Server Client sends instructions to the control unit of can-type calcine furnace, the control of can-type calcine furnace
Unit processed sends instructions to described air conditioner;Selectively, send instructions to described draft regulator.
After employing technique scheme, can-type calcine furnace discharging temperature control device of the present utility model includes being arranged on pot type
The photoelectric temperature sensor of calcining furnace quirk, it is arranged on the air conditioner of can-type calcine furnace air channel entrance and is arranged on pot type
The draft regulator of calcinator aggregated flue outlet, photoelectric temperature sensor, air conditioner and draft regulator respectively with tank
The control unit electrical connection of formula calcining furnace.The quirk real time temperature signal of detection is sent to pot type calcining by photoelectric temperature sensor
The control unit of stove, when quirk real time temperature is higher than quirk target temperature, the control unit of can-type calcine furnace sends instructions to
Air conditioner, reduces the open degree of air conditioner, reduces the air inlet amount entering quirk from air channel, reduces in quirk
The burning degree of fugitive constituent, reduces quirk real time temperature, until quirk real time temperature is down to quirk target temperature;Selectively,
The control unit of can-type calcine furnace also sends instructions to draft regulator, the open degree of intensified negative pressure actuator, increases high temperature cigarette
Gas gas output, contributes to quickly reducing quirk real time temperature, shortens quirk real time temperature and is down to the time used by quirk target temperature.
When quirk real time temperature is less than quirk target temperature, the control unit of can-type calcine furnace sends instructions to air conditioner, plus
The open degree of big air conditioner, increases the air inlet amount entering quirk from air channel, improves the burning of fugitive constituent in quirk
Degree, raises quirk real time temperature, until quirk real time temperature rises to quirk target temperature;Selectively, can-type calcine furnace
Control unit also sends instructions to draft regulator, reduces the open degree of draft regulator, reduces high-temperature flue gas gas output, helps
Raise quirk real time temperature in quick, shorten quirk real time temperature and rise to the time used by quirk target temperature.Achieve to pot type
The scene of calcining furnace homoiothermic automatically controls.
Control unit due to can-type calcine furnace is also connected with remote client's end communication, and the control unit of can-type calcine furnace can
So that the indexs such as the temperature of can-type calcine furnace, air, negative pressure are uploaded Terminal Server Client, Terminal Server Client sends instructions to pot type and forges
Burn the control unit of stove, the control unit of can-type calcine furnace sends instructions to air conditioner, draft regulator it is achieved that not
Same region, the remote auto control to can-type calcine furnace homoiothermic for the different time.
In sum, can-type calcine furnace discharging temperature control device of the present utility model and its control method are it is achieved that to pot type
Accurately automatically controlling of calcining furnace homoiothermic, improves the use longevity of calcining furnace while improve calcined petroleum coke product quality
Life;By improving the automaticity of can-type calcine furnace, reduce cost of labor;Can-type calcine furnace achieves remotely control, pole
The earth improves the working environment of workman.
Brief description
Fig. 1 is the can-type calcine furnace discharging temperature control device structural representation of this utility model embodiment;
Fig. 2 is the homoiothermic control method flow chart of the can-type calcine furnace discharging temperature control device of this utility model embodiment;
In figure:1- hopper;2- tank body;3- fugitive constituent road;4- collection flue;5- quirk;6- air channel;7- air adjustment
Device;8- photoelectric temperature sensor;9- flue gas pressures table;10- draft regulator.
Specific embodiment
Below in conjunction with the accompanying drawings further non-limitative illustration is done to specific embodiment of the present utility model.
As shown in figure 1, the can-type calcine furnace in this utility model includes tank body 2, the top of tank body 2 is provided with hopper 1, tank body
The collection flue 4 that the air channel 6 that 2 outside is provided with fugitive constituent road 3, quirk 5 is connected with quirk 5 is connected with bottom quirk.This
The can-type calcine furnace discharging temperature control device of utility model includes:It is arranged on the photoelectric temperature sensor of the quirk 5 of can-type calcine furnace
8th, the air conditioner 7 of air channel 6 entrance being arranged on can-type calcine furnace and the collection flue 4 being arranged on can-type calcine furnace export
Draft regulator 10, collection flue 4 is also equipped with flue gas pressures table 9, photoelectric temperature sensor 8, air conditioner 7, negative
Pressure actuator 10 is electrically connected (in figure is not specifically illustrated) with the control unit of can-type calcine furnace respectively;Further, pot type calcining
The control unit of stove is also connected (as shown in Figure 2) with remote client's end communication.
As shown in Fig. 2 the homoiothermic control method of can-type calcine furnace discharging temperature control device of the present utility model is as follows:
For example, setting can-type calcine furnace has five temperature gears:1150 ± 20 DEG C, 1200 ± 20 DEG C, 1250 ± 20 DEG C,
1300 ± 20 DEG C, 1350 ± 20 DEG C;For each temperature gear, its homoiothermic control method step is as follows:
Set quirk target temperature as T0;
Photoelectric temperature sensor 8 detection quirk 5 real time temperature is T1, and real time temperature signal is sent to can-type calcine furnace
Control unit;
Real time temperature T1 and target temperature T0 is compared and judges and send instruction by the control unit of can-type calcine furnace:
If T1 is > T0, the control unit of can-type calcine furnace sends instructions to air conditioner 7, reduces air conditioner 7
Open degree, reduces the air inlet amount entering quirk 5 from air channel 6, reduces the burning degree of fugitive constituent in quirk 5, reduce fire
Road 5 real time temperature, until quirk 5 real time temperature is down to quirk target temperature;Selectively, the control unit of can-type calcine furnace is also
Send instructions to draft regulator 10, the open degree of intensified negative pressure actuator 10, the high-temperature flue gas increasing collection flue 4 are given vent to anger
Amount, contributes to quickly reducing quirk real time temperature, shortens quirk real time temperature and is down to the time used by quirk target temperature;According to reality
Border situation, the control unit of can-type calcine furnace can not also send instructions to draft regulator 10 it is not necessary to adjust draft regulator
10 open degree, the only open degree by reducing air conditioner 7 reduce the purpose of quirk 5 real time temperature.
If T1 is < T0, the control unit of can-type calcine furnace sends instructions to air conditioner 7, increase air actuator 7
Open degree, increases the air inlet amount entering quirk 5 from air channel 6, improves the burning degree of fugitive constituent in quirk 5, raise fire
Road 5 real time temperature, until quirk 5 real time temperature rises to quirk target temperature;Selectively, the control unit of can-type calcine furnace is also
Send instructions to draft regulator 10, reduce the open degree of draft regulator 10, the high-temperature flue gas reducing collection flue 4 are given vent to anger
Amount, contributes to quickly raising quirk real time temperature, shortens quirk real time temperature and rises to the time used by quirk target temperature.According to reality
Border situation, the control unit of can-type calcine furnace can not also send instructions to draft regulator 10 it is not necessary to adjust draft regulator
10 open degree, only reaches, by the open degree of increase air actuator 7, the purpose raising quirk 5 real time temperature.
The scene that above homoiothermic control method step achieves to can-type calcine furnace homoiothermic automatically controls.
As shown in Fig. 2 due to can-type calcine furnace control unit also with Terminal Server Client (such as mobile phone, panel computer etc.
Mobile client, or the desktop computer as host computer) communication connection, can realize pot type is calcined by Terminal Server Client
The remote auto control of stove homoiothermic:The control unit of can-type calcine furnace is by the indexs such as the temperature of can-type calcine furnace, air, negative pressure
Pass Terminal Server Client, Terminal Server Client sends instructions to the control unit of can-type calcine furnace, and the control unit of can-type calcine furnace is sent out
Send instruction to air conditioner 7, draft regulator 10 in order to control respective open degree, adjust quirk 5 real time temperature, until fire
Road 5 real time temperature reach quirk target temperature it is achieved that different geographical, different time to can-type calcine furnace homoiothermic long-range from
Dynamic control;Manager regardless of the operation of region, remote monitoring can-type calcine furnace regardless of time, and a people can manage multiple stage pot type
Calcining furnace, has saved human cost, significantly improves working environment.
Claims (2)
1. can-type calcine furnace discharging temperature control device is it is characterised in that include:
Photoelectric temperature sensor, described photoelectric temperature sensor is arranged on the quirk of can-type calcine furnace;
Air conditioner, described air conditioner is arranged on the air channel entrance of described can-type calcine furnace;
Draft regulator, described draft regulator is arranged on the collection flue outlet of described can-type calcine furnace;
The control with described can-type calcine furnace respectively of described photoelectric temperature sensor, described air conditioner, described draft regulator
Unit electrical connection processed.
2. can-type calcine furnace discharging temperature control device as claimed in claim 1 is it is characterised in that the control of described can-type calcine furnace
Unit is also connected with remote client's end communication.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620738362.5U CN205933242U (en) | 2016-07-13 | 2016-07-13 | Pot calciner temperature -adjusting control device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620738362.5U CN205933242U (en) | 2016-07-13 | 2016-07-13 | Pot calciner temperature -adjusting control device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN205933242U true CN205933242U (en) | 2017-02-08 |
Family
ID=57929047
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201620738362.5U Active CN205933242U (en) | 2016-07-13 | 2016-07-13 | Pot calciner temperature -adjusting control device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN205933242U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106044746A (en) * | 2016-07-13 | 2016-10-26 | 潍坊联兴新材料科技股份有限公司 | Pot calciner thermoregulation control device and method |
CN109028991A (en) * | 2018-05-02 | 2018-12-18 | 太仓北新建材有限公司 | Control method, device and the calcining furnace of negative pressure in a kind of calcining furnace |
-
2016
- 2016-07-13 CN CN201620738362.5U patent/CN205933242U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106044746A (en) * | 2016-07-13 | 2016-10-26 | 潍坊联兴新材料科技股份有限公司 | Pot calciner thermoregulation control device and method |
CN109028991A (en) * | 2018-05-02 | 2018-12-18 | 太仓北新建材有限公司 | Control method, device and the calcining furnace of negative pressure in a kind of calcining furnace |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106044746B (en) | Can-type calcine furnace discharging temperature control device and its temperature adjustment control method | |
CN105159235B (en) | Calcination process in rotary kiln synthesizes and coordinates control method and system | |
CN102721104B (en) | Central heating system supply water temperature weather compensation control method | |
CN205933242U (en) | Pot calciner temperature -adjusting control device | |
CN102053562B (en) | Cracking furnace exit temperature hybrid control method | |
CN107655345A (en) | A kind of intelligent temperature control system and temperature control method for calcining stove | |
CN204881149U (en) | Manganese zinc fritting furnace for ferrite material | |
CN102134727A (en) | Method for recycling waste heat of electrolytic cell and device thereof | |
CN207584816U (en) | The coefficient of excess air management system of kiln | |
CN105509498B (en) | Pot type burner automatic temperature control | |
CN206177055U (en) | Electric stove high temperature smoke and dust utilizes and dust collector | |
CN206902250U (en) | A kind of heat preservation of aluminium electrolytic cell regulation and afterheat utilizing system | |
CN116499272B (en) | Intelligent kiln control method for tracking multi-energy combustion carbon emission | |
CN109539812A (en) | A kind of sleeve kiln intelligent gas controlling device and control method | |
CN202329260U (en) | Kiln observation hole | |
CN107726847B (en) | It is a kind of for calcining the temperature intelligent adjusting method of stove | |
CN203240767U (en) | Hot blast stove combustion optimal control system | |
CN102540883A (en) | Intelligent optimized energy saving and emission reducing controlling system | |
CN108072282B (en) | A kind of annular lime kiln calcining autocontrol method | |
CN201347360Y (en) | Calcining furnace with two carbon calcining manners | |
CN205710951U (en) | Metallurgical furnace kiln numeral calciner | |
CN204944156U (en) | A kind of production carbide alloy hot pressing furnace | |
CN108977206A (en) | A kind of quenching furnace prestores the control pressurer system of room | |
CN201826022U (en) | Aluminum electrolysis cell gas roasting device | |
CN103713600B (en) | Automatic control system for producing potash fertilizer |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
PP01 | Preservation of patent right | ||
PP01 | Preservation of patent right |
Effective date of registration: 20201221 Granted publication date: 20170208 |
|
PD01 | Discharge of preservation of patent | ||
PD01 | Discharge of preservation of patent |
Date of cancellation: 20231221 Granted publication date: 20170208 |