CN201065437Y - Temperature control device for electrolysis bath binding groove cathode carbon block heating system - Google Patents
Temperature control device for electrolysis bath binding groove cathode carbon block heating system Download PDFInfo
- Publication number
- CN201065437Y CN201065437Y CNU2007201230773U CN200720123077U CN201065437Y CN 201065437 Y CN201065437 Y CN 201065437Y CN U2007201230773 U CNU2007201230773 U CN U2007201230773U CN 200720123077 U CN200720123077 U CN 200720123077U CN 201065437 Y CN201065437 Y CN 201065437Y
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- heating
- control device
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- 238000010438 heat treatment Methods 0.000 title claims abstract description 69
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 64
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 64
- 238000005868 electrolysis reaction Methods 0.000 title 1
- 239000011449 brick Substances 0.000 claims description 8
- 238000001514 detection method Methods 0.000 abstract description 13
- 238000000034 method Methods 0.000 abstract description 9
- 210000005056 cell body Anatomy 0.000 description 17
- 210000004027 cell Anatomy 0.000 description 14
- 238000005516 engineering process Methods 0.000 description 11
- 238000013461 design Methods 0.000 description 10
- 239000002562 thickening agent Substances 0.000 description 9
- 238000012360 testing method Methods 0.000 description 7
- 230000003245 working effect Effects 0.000 description 4
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical compound [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 3
- 239000004411 aluminium Substances 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 206010034703 Perseveration Diseases 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 238000005553 drilling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 230000001932 seasonal effect Effects 0.000 description 2
- 241001044684 Amadina fasciata Species 0.000 description 1
- 229910000754 Wrought iron Inorganic materials 0.000 description 1
- 230000036760 body temperature Effects 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 235000000396 iron Nutrition 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 230000011218 segmentation Effects 0.000 description 1
- 230000002277 temperature effect Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
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Abstract
The utility model discloses a heating system temperature control device for rammed cathode carbon block in electrolytic bath, comprising a heating device and temperature detection devices; the utility model is characterized in that: cathode carbon blocks (2) are positioned at the bottom of an electrolytic bath (1), a lateral carbon block (6) is provided at lateral face of the electrolytic bath (1); the cathode carbon block (2) that is arranged inside the electrolytic bath (1) is divided at least into two areas, independent heating devices are arranged on the cathode carbon blocks (2) of each area respectively and the temperature detection devices are arranged on cathode carbon blocks (2) of each area. The utility model has the advantages that the device solves the problems of great temperature difference of each part due to the different heating temperature of the carbon blocks at bottom of the bath and the lateral carbon blocks during the overhaul process of each type of electrolytic bath and the optimal bath-ramming temperature and ramming effectiveness between the bath body cathode block and the paste can be achieved which can thus prolong the service life of the cathode block.
Description
Technical field
The utility model relates to a kind of temperature-control device of electrolytic cell binding groove cathode carbon block heating system, temperature control technology field when belonging to aluminium cell bundle groove.
Background technology
In electrolytic cell overhaul, it is to prick groove technology that one important operation arranged, and the homo(io)thermism control of cell body heating in this technology can produce great effect to the last quality of electrolytic cell binding groove.In the prior art, the watt level of aluminium cell is relevant with the cathode block quantity of bottom land, and the cathode block quantity of common aluminium cell is usually between 15～21.Prick groove technology be meant cathode block is placed on the bottom land of electrolyzer after, need be coated with around the cell body and the gap between the cathode block full with thickener.And therefore the temperature of pricking the groove thickener needs the carbon piece is heated before pricking groove usually at 90～110 ℃, makes that the temperature of carbon piece and thickener is identical.Prior art adopts many group well heater anticathode carbon pieces to heat, one group of well heater (one group of well heater is made up of 30 heating pieces) is set in the slit between per two cathode blocks, the well heater of all cathode blocks adopts a device control, control accuracy is low, adopts continuous type of heating, waste heat energy, in case and heating installation is out of order, lean on the maintenance worker from the heating piece of four or five hundred of more than ten groups, to find out the trouble spot, need a lot of times, strengthen labor strength.Temperature detection also is to detect on the cathode block next door by temperature measuring equipment, is perhaps judged poor accuracy by experience by the workman.And prick cell body Heating temperature in the groove technology in reality and can change to some extent with the change of the difference in season and envrionment temperature, and the temperature rise of the different sites Heating temperature of cell body is again nonsynchronous, depend merely on manually and control, want in Various Seasonal, under the varying environment temperature, the temperature at each position of cell body is heated to the temperature of pricking the groove processing requirement, make bottom of electrolytic tank carbon piece identical with bundle groove thickener temperature with the sidewall carbon brick Heating temperature, reaching best adhesive effect is to be difficult to realize, roasting groove temperature often occurring can't accurately grasp, sometimes even above processing requirement temperature more than 20 spend, come difficulty for the thickener wrapping-fixed belt, the groove quality is pricked in influence, thereby influences the work-ing life of electrolyzer.
Summary of the invention
The purpose of this utility model is: a kind of temperature control precision height is provided, can changes, solve the nonsynchronous problem of temperature rise of the different sites Heating temperature of cell body along with the variation of envrionment temperature, realized cathode block before the electrolytic cell binding groove, the temperature-control device of the electrolytic cell binding groove cathode carbon block heating system of lateral mass heating system on every side, made each bottom carbon piece of electrolyzer and sidewall carbon brick Heating temperature reach the best groove technological temperature requirement of pricking.
The utility model is achieved in that it comprises electrolyzer 1, in electrolyzer 1 bottom cathode block 2 is set, be provided with sidewall carbon brick 6 in electrolyzer 1 side, cathode block 2 in the electrolyzer 1 is divided into 2 zones at least, each regional cathode block 2 is provided with independently heating unit, is provided with temperature-detecting device on each regional cathode block 2.Cathode block 2 in the electrolyzer 1 is divided into 3～8 zones, and each zone comprises 2～10 cathode blocks 2.Cathode block 2 in the electrolyzer 1 is divided into 3～5 zones, and each zone comprises 4～8 cathode blocks 2.The structure of heating unit comprises and is located at the well heater in the slit 7 between the cathode block 2 that each regional well heater 7 connects a control device 8.The structure of temperature-detecting device comprises thermometric carbon piece 5, is provided with the hole on thermometric carbon piece 5, is provided with the hot resistance that thermometric is used in the hole, and thermometric carbon piece 5 is placed on the medium position of each regional intermediary cathode block 2.The length of thermometric carbon piece 5 be 100～200 millimeters, wide be that 50～150 millimeters, height are 100～200 millimeters, the diameter in hole is 5～10 millimeters, hole depth is 70～180 millimeters.
The utility model is that the applicant works for many years and tests, in the electrolytic cell overhaul operation.At pricking the problem that groove technology upper groove body Heating temperature can change to some extent with the change of the difference in season and envrionment temperature,, find out the method and apparatus of best control flume body temperature degree in conjunction with actual production technology.When the bundle groove heated the electrolyzer cell body, the temperature rise of different sites was inequality, measured in real work and found that cell body two ends temperature rise is slower, and the middle part temperature rise is very fast, 27 ℃ of maximum temperature differences, 15.4 ℃ of mean temperature difference, the big like this temperature difference directly influences the quality of overhaul electrolytic cell binding groove.Therefore the utility model adopts relatively independent subregion heating control apparatus, difference according to temperature, cell body is divided into a plurality of zones, be generally 3～8 zones, using independently respectively, the temperature automatic heating device heats these regional cathode blocks and controls, the controlled temperature in a plurality of zones is provided with identical value, makes that the temperature at actual heating cell body two ends and middle part is identical, thereby eliminated the influence that causes because of the cell body different sites heating temperature difference.Simultaneously,, only need this regional heating piece is detected, needn't detect the heating piece of whole electrolyzer, reduced workload if there is certain regional heating piece to damage.
The applicant is in conjunction with actual production, and design alternative optimal detection point and the proofing unit that is complementary with it solve and measure temperature and the consistent problem of carbon piece actual temperature.Through test of many times, choosing each regional optimum detection position is the middle part of the cathode block in each regional mid-way.
Through test of many times, proofing unit is selected three little carbon pieces of processing, material is identical with bottom of electrolytic tank carbon piece, every block length be 100～200 millimeters, wide be that 50～150 millimeters, height are 100～200 millimeters, the diameter of boring is 5～10 millimeters respectively on every carbon piece, hole depth is 70～180 millimeters one of a circular hole, during monitoring hot resistance is inserted in the hole gently, then little carbon piece is placed on each regional optimum detection position of bottom of electrolytic tank respectively reposefully, like this can be so that the error of detected temperatures and cathode block actual temperature reaches minimum.
Simultaneously, because the heating of cathode block need be kept 12 hours usually, continue a night, therefore the utility model can also rationally be selected the warning dead band of temperature instrument for use, through repetition test, sum up the time and the set(ting)value of warning dead band, promptly that night 20:00------4:00 next day warning dead band be transferred to 5 the degree, during this period of time promptly, after the temperature of cathode block heating and the temperature difference of design temperature had surpassed 5 degree, temperature instrument was just reported to the police, equipment action at this moment, stopping anticathode carbon piece heats, after the temperature difference of the temperature of cathode block heating and design temperature was lower than 5 degree, anticathode carbon piece heated again, thereby the temperature that control cathode carbon piece heats is in set temperature value ± 5 degree scopes, reach and prolong stopping of cathode block heating, electric power feeding time has reduced the perseveration and the heat energy loss of equipment.4:00------8:00 promptly is transferred to 0.1 in next day, during this period of time promptly, the temperature of cathode block heating and the temperature difference of design temperature have surpassed 0.1 degree, equipment stops anticathode carbon piece and heats, heat when design temperature 0.1 is spent when being lower than, thereby the homo(io)thermism of control cathode carbon piece heating has improved the precision of cathode block Heating temperature in set temperature value ± 0.1 degree scope, and the Heating temperature when guaranteeing the second bundle groove reaches the optimised process requirement.Can reduce the heating energy consumption like this, can prolong the work-ing life of contactor again, simultaneously, can also guarantee that the cathode block Heating temperature reaches the optimised process requirement of setting.
The utility model has solved in the various electrolytic cell overhaul process, the different big shortcomings of each position temperature difference that cause of cell body each carbon piece of bottom with the sidewall carbon brick Heating temperature, regulate the influence of Various Seasonal and envrionment temperature to the cell body Heating temperature, make to reach best between cell body carbon piece and the thickener and prick groove technological temperature and adhesive effect, thus prolonging overhaul electrolyzer work-ing life; Simultaneously, also take the intermittent type heating, save energy; Design utilizes instrument, instrument tracing trouble position, dwindles the handling failure time, alleviates labor strength.Along with the market cut-throat competition, each enterprise will update overhaul electrolyzer technology, to pricking the whole Heating temperature of groove technology cell body requirements at the higher level can be proposed, the research and development of controlling at the whole heating of electrolytic cell overhaul operation-Zha groove technology cell body, segmentation is not specially also arranged at present, and this utility model just in time solves the temperature control needs of each enterprise to cell body whole constant temperature heating in the electrolytic cell overhaul process, forward-looking, advanced, the needs that meet enterprise development have excellent popularization prospect and vast market space.
Description of drawings
Accompanying drawing 1 is a structural representation of the present utility model;
Accompanying drawing 2 is the D-D sectional view of accompanying drawing 1.
Reference numeral: 1-electrolyzer, 2-cathode block, 3-thickener, 4-rod iron, 5-thermometric carbon piece, 6-sidewall carbon brick, 7-well heater, 8-control device.
Embodiment
The structure of the heating unit that cathode block 2 adopts comprises and is located at the well heater in the slit 7 between the cathode block 2, well heater 7 is made up of 30 heating pieces, each regional well heater 7 connects a control device 8, so just the heating unit in A, B, C zone is independently controlled and is operated.The structure of temperature-detecting device comprises thermometric carbon piece 5, and drilling bore hole on thermometric carbon piece 5 inserts the hot resistance that thermometric is used in the hole, thermometric carbon piece 5 is placed on the medium position of each regional intermediary cathode block 2.
According to the size of electrolyzer 1 and cathode block 2 quantity what, the cathode block 2 in the electrolyzer 1 can be divided into 3～8 zones, each zone comprises 2～10 cathode blocks 2.Through applicant's repetition test, scheme is that the cathode block 2 in the electrolyzer 1 is divided into 3～5 zones preferably, each zone comprises 4～8 cathode blocks 2, so both can guarantee that cathode block 2 temperature in each zone were more or less the same, can not increase too many operating device again, improve plant factor, reduce production costs.
Through applicant's repetition test, anticathode carbon piece 2 carries out the middle part of the optimal site of temperature detection for each regional mid-way cathode block 2.Adopt the method for temperature detection to be, produce thermometric carbon piece 5 with the same material of cathode block, drilling bore hole on thermometric carbon piece 5 inserts in the hole hot resistance during monitoring gently, then thermometric carbon piece 5 is placed on each regional optimum detection position of bottom of electrolytic tank respectively reposefully.In order to guarantee heat-transfer effect, the length of every thermometric carbon piece 5 be 100～200 millimeters, wide be that 50～150 millimeters, height are 100～200 millimeters, the diameter in hole is 5～10 millimeters, hole depth is 70～180 millimeters.As shown in Figure 1, the optimal site of A, B, the detection of C regional temperature is the middle part that the 2nd, the 8th, the 15th cathode block 2 played on electrolyzer 1 left side.The optimal site of temperature detection also can be the middle part of electrolyzer 1 left side the 3rd, the 9th, the 14th cathode block 2.
Applicant of the present utility model is through repetition test, sum up the duration of service and the set(ting)value of temperature instrument warning dead band, promptly that night 20:00------4:00 next day warning dead band be transferred to 5 the degree, during this period of time promptly, after the temperature of cathode block heating and the temperature difference of design temperature have surpassed 5 degree, temperature instrument is just reported to the police, at this moment equipment action, stopping anticathode carbon piece heats, when the temperature difference of the temperature of cathode block heating and design temperature be lower than 5 spend after, anticathode carbon piece heats again, thereby the temperature of control cathode carbon piece heating is in set temperature value ± 5 degree scopes, reach and prolong stopping of cathode block heating, electric power feeding time has reduced the perseveration and the heat energy loss of equipment.4:00------8:00 promptly is transferred to 0.1 in next day, during this period of time promptly, the temperature of cathode block heating and the temperature difference of design temperature have surpassed 0.1 degree, equipment stops anticathode carbon piece and heats, heat when design temperature 0.1 is spent when being lower than, thereby the homo(io)thermism of control cathode carbon piece heating has improved the precision of cathode block Heating temperature in set temperature value ± 0.1 degree scope, and the Heating temperature when guaranteeing the second bundle groove reaches the optimised process requirement.Can reduce the heating energy consumption like this, can prolong the work-ing life of contactor again, simultaneously, can also guarantee that the cathode block Heating temperature reaches the optimised process requirement of setting.
Heating unit that each is regional and temperature-detecting device such as embodiment 1.
Claims (6)
1. the temperature-control device of an electrolytic cell binding groove cathode carbon block heating system, it comprises electrolyzer (1), it is characterized in that: cathode block (2) is set in electrolyzer (1) bottom, be provided with sidewall carbon brick (6) in electrolyzer (1) side, cathode block (2) in the electrolyzer (1) is divided into 2 zones at least, each regional cathode block (2) is provided with independently heating unit, is provided with temperature-detecting device on each regional cathode block (2).
2. the temperature-control device of electrolytic cell binding groove cathode carbon block heating system according to claim 1 is characterized in that: the cathode block (2) in the electrolyzer (1) is divided into 3～8 zones, and each zone comprises 2～10 cathode blocks (2).
3. the temperature-control device of electrolytic cell binding groove cathode carbon block heating system according to claim 2 is characterized in that: the cathode block (2) in the electrolyzer (1) is divided into 3～5 zones, and each zone comprises 4～8 cathode blocks (2).
4. the temperature-control device of electrolytic cell binding groove cathode carbon block heating system according to claim 1, it is characterized in that: the structure of heating unit comprises and is located at the well heater (7) in the slit between the cathode block (2) that each regional well heater (7) connects control device (8).
5. the temperature-control device of electrolytic cell binding groove cathode carbon block heating system according to claim 1, it is characterized in that: the structure of temperature-detecting device comprises thermometric carbon piece (5), on thermometric carbon piece (5), be provided with the hole, be provided with the hot resistance that thermometric is used in the hole, thermometric carbon piece (5) is placed on the medium position of each regional intermediary cathode block (2).
6. the temperature-control device of electrolytic cell binding groove cathode carbon block heating system according to claim 5, it is characterized in that: the length of thermometric carbon piece (5) be 100～200 millimeters, wide be that 50～150 millimeters, height are 100～200 millimeters, the diameter in hole is 5～10 millimeters, and hole depth is 70～180 millimeters.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201230773U CN201065437Y (en) | 2007-06-20 | 2007-06-20 | Temperature control device for electrolysis bath binding groove cathode carbon block heating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201230773U CN201065437Y (en) | 2007-06-20 | 2007-06-20 | Temperature control device for electrolysis bath binding groove cathode carbon block heating system |
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| Publication Number | Publication Date |
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| CN201065437Y true CN201065437Y (en) | 2008-05-28 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNU2007201230773U Expired - Lifetime CN201065437Y (en) | 2007-06-20 | 2007-06-20 | Temperature control device for electrolysis bath binding groove cathode carbon block heating system |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101328596B (en) * | 2007-06-20 | 2010-06-30 | 中国铝业股份有限公司 | Temperature control method and apparatus of electrolytic cell binding groove cathode carbon block heating system |
| CN101748434B (en) * | 2008-12-11 | 2012-07-04 | 中国铝业股份有限公司 | Fixing method of electrolytic bath and heating device for fixture of electrolytic bath |
| CN103243351A (en) * | 2013-05-20 | 2013-08-14 | 中南大学 | Region electrolysis prebaking aluminum cell |
| CN106400054A (en) * | 2016-06-24 | 2017-02-15 | 沈阳汇丰机械有限公司 | Cathode assembling preheating station |
-
2007
- 2007-06-20 CN CNU2007201230773U patent/CN201065437Y/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101328596B (en) * | 2007-06-20 | 2010-06-30 | 中国铝业股份有限公司 | Temperature control method and apparatus of electrolytic cell binding groove cathode carbon block heating system |
| CN101748434B (en) * | 2008-12-11 | 2012-07-04 | 中国铝业股份有限公司 | Fixing method of electrolytic bath and heating device for fixture of electrolytic bath |
| CN103243351A (en) * | 2013-05-20 | 2013-08-14 | 中南大学 | Region electrolysis prebaking aluminum cell |
| CN103243351B (en) * | 2013-05-20 | 2016-08-03 | 中南大学 | A kind of subregion electrolysis pre-calcining electrolytic cell |
| CN106400054A (en) * | 2016-06-24 | 2017-02-15 | 沈阳汇丰机械有限公司 | Cathode assembling preheating station |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20080528 Effective date of abandoning: 20070620 |