CN102107894A - Alumina clinker cooling device - Google Patents
Alumina clinker cooling device Download PDFInfo
- Publication number
- CN102107894A CN102107894A CN 200910312442 CN200910312442A CN102107894A CN 102107894 A CN102107894 A CN 102107894A CN 200910312442 CN200910312442 CN 200910312442 CN 200910312442 A CN200910312442 A CN 200910312442A CN 102107894 A CN102107894 A CN 102107894A
- Authority
- CN
- China
- Prior art keywords
- control unit
- pipeline
- electrically connected
- plc control
- cooler
- 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
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 title claims abstract description 20
- 238000001816 cooling Methods 0.000 title claims abstract description 9
- 238000000034 method Methods 0.000 claims description 5
- 230000000694 effects Effects 0.000 abstract description 3
- 238000009529 body temperature measurement Methods 0.000 abstract 2
- 238000010992 reflux Methods 0.000 abstract 2
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 4
- 238000010517 secondary reaction Methods 0.000 description 4
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 4
- 229910001948 sodium oxide Inorganic materials 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Furnace Details (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
The invention discloses an alumina clinker cooling device. A centrifugal pump (7) is arranged on a pipeline (1), an electric reflux valve (2) is connected at the inlet or outlet end of the centrifugal pump (7), a gate valve (6) and an electric main valve (8) are connected on the inlet or outlet pipeline of the centrifugal pump (7) respectively, a nozzle (11) is connected at the end of a pipeline (1) and extends into the outlet of a cooler (12), a flow meter (9) and a pressure gauge (red 10) are arranged on the pipeline (1) between the electric main valve (8) and the nozzle (11), and an external line temperature measurement instrument (5) is arranged at the outlet of the cooler (12); the flow meter (9), the pressure gauge (10) and the external line temperature measurement instrument (5) are electrically connected with a programmable logic controller (PLC) control unit (3); and the PLC control unit (3) is electrically connected with a microcomputer (4). The electric reflux valve (2) and the electric main valve (8) are electrically connected with the PLC control unit (3). The device has remarkable cooling effect, strong clinker temperature controllability and capability of reclaiming clinker heat.
Description
Technical field
The present invention relates to a kind of alumina clinker heat sink, belong to grog cooling technique equipment field in the alumina producing sintering circuit.
Background technology
At present, alumina clinker heat sink of the prior art is that the slight negative pressure that the outlet of trickle and cooler produces outside the cooler cylindrical shell will be lowered the temperature to alumina clinker in the air suction cooler, because of cooling-down effect poor, usually the alumina clinker temperature can be reduced to 320 ℃ ± 60 ℃ by 1000 ℃, but clinker temperature is still higher, do not reach production requirement below 230 ℃, make on the one hand and enter stripping of next procedure grog and settlement separate alumina clinker temperature drift, directly cause aluminum oxide and the loss of sodium oxide secondary reaction in the grog to increase; Clinker temperature is higher on the other hand, and the heat of directly taking away can't reclaim, and calorific loss is bigger.
Summary of the invention
The technical problem to be solved in the present invention is: a kind of alumina clinker heat sink is provided, this device can make the alumina clinker cooling, can reclaim the part heat that grog is taken away again, the alumina clinker temperature is lower than below 230 ℃, greatly reduce grog in stripping and aluminum oxide and the loss of sodium oxide secondary reaction when settlement separate, to overcome deficiencies such as alumina clinker temperature drift, calorific loss that prior art exists are bigger.
The present invention constitutes like this: it comprises pipeline 1, electronic reverse flow valve 2, PLC control unit 3, microcomputer 4, infrared thermometer 5, gate valve 6, impeller pump 7, electronic main valve 8, under meter 9, tensimeter 10, nozzle 11, cooler 12, impeller pump 7 is installed on pipeline 1, electronic reverse flow valve 2 is connected impeller pump 7 and advances, exit end, gate valve 6 and electronic main valve 8 are connected to impeller pump 7 and advance, on the outlet conduit, nozzle 11 is connected pipeline 1 termination and stretches into cooler 12 outlet the insides, under meter 9, tensimeter 10 is installed on the pipeline 1 between electronic main valve 8 and the nozzle 11, and outside line temperature measurer 5 is installed in cooler 12 exits; Under meter 9, tensimeter 10, outside line temperature measurer 5 are electrically connected with PLC control unit 3, and PLC control unit 3 is electrically connected with microcomputer 4.
Electronic reverse flow valve 2 is electrically connected with PLC control unit 3.
Electronic main valve 8 is electrically connected with PLC control unit 3.
During work, under meter 9, tensimeter 10, infrared thermometer 5 detects numerical value and regulates control by PLC control unit 3 and 4 pairs of electronic reverse flow valves 2 of microcomputer, electronic main valve 8 apertures, the alumina clinker temperature and the electronic main valve 8 apertures interlocking of 12 outlets of infrared thermometer 5 monitoring coolers, cooler 12 stops and electronic reverse flow valve 2, electronic main valve 8 apertures interlocking, tensimeter 10 monitoring pressure data and electronic reverse flow valve 2 apertures interlocking.
The present invention lowers the temperature to alumina clinker by spray cyclic regeneration water, can reclaim the part heat that grog is taken away, can rapidly and efficiently lower the temperature again, the alumina clinker temperature is lower than below 230 ℃, greatly reduce grog in stripping and aluminum oxide and the loss of sodium oxide secondary reaction when settlement separate; And can concentrate recycling to waste gas from the opening for feed of cooler.
Compared with prior art, the present invention has advantages such as cooling-down effect is remarkable, the clinker temperature controllability is strong, the grog heat can reclaim, use the present invention can guarantee that the alumina clinker cooling meets production requirement, greatly reduce grog and lose at stripping aluminum oxide and sodium oxide secondary reaction when settlement separate.
Description of drawings
Fig. 1 is a structure connection diagram of the present invention.
Embodiment
Embodiments of the invention: anticipate as shown in Figure 1, the present invention includes pipeline 1, electronic reverse flow valve 2, PLC control unit 3, microcomputer 4, infrared thermometer 5, gate valve 6, impeller pump 7, electronic main valve 8, under meter 9, tensimeter 10, nozzle 11, cooler 12, impeller pump 7 is installed on pipeline 1, electronic reverse flow valve 2 is connected impeller pump 7 and advances, exit end, gate valve 6 and electronic main valve 8 are connected to impeller pump 7 and advance, on the outlet conduit, nozzle 11 is connected pipeline 1 termination and stretches into cooler 12 outlet the insides, under meter 9, tensimeter 10 is installed on the pipeline 1 between electronic main valve 8 and the nozzle 11, and outside line temperature measurer 5 is installed in cooler 12 exits; Under meter 9, tensimeter 10, outside line temperature measurer 5 are electrically connected with PLC control unit 3, and PLC control unit 3 is electrically connected with microcomputer 4.
Electronic reverse flow valve 2 is electrically connected with PLC control unit 3.
Electronic main valve 8 is electrically connected with PLC control unit 3.
Claims (3)
1. alumina clinker cooling technique device, it comprises cooler (12), nozzle (11), it is characterized in that: go up at pipeline (1) impeller pump (7) is installed, electronic reverse flow valve (2) is connected impeller pump (7) and advances, exit end, gate valve (6) and electronic main valve (8) are connected to impeller pump (7) and advance, on the outlet conduit, nozzle (11) is connected pipeline (1) termination and stretches into cooler (12) outlet the inside, under meter (9), tensimeter (red 10) is installed on the pipeline (1) between electronic main valve (8) and the nozzle (11), and outside line temperature measurer (5) is installed in cooler (12) exit; Under meter (9), tensimeter (10), outside line temperature measurer (5) are electrically connected with PLC control unit (3), and PLC control unit (3) is electrically connected with microcomputer (4).
2. alumina clinker cooling technique device according to claim 1 is characterized in that: electronic reverse flow valve (2) is electrically connected with PLC control unit (3).
3. alumina clinker cooling technique device according to claim 1 is characterized in that: electronic main valve (8) is electrically connected with PLC control unit (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200910312442 CN102107894B (en) | 2009-12-28 | 2009-12-28 | Alumina clinker cooling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200910312442 CN102107894B (en) | 2009-12-28 | 2009-12-28 | Alumina clinker cooling device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102107894A true CN102107894A (en) | 2011-06-29 |
| CN102107894B CN102107894B (en) | 2013-01-02 |
Family
ID=44172192
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200910312442 Active CN102107894B (en) | 2009-12-28 | 2009-12-28 | Alumina clinker cooling device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102107894B (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101289289A (en) * | 2007-07-13 | 2008-10-22 | 襄樊金和环保科技有限公司 | Quenching, temperature-reducing and self-controlling device for chamotte of energy-conserving rotating stove |
| CN201230256Y (en) * | 2008-07-11 | 2009-04-29 | 广州德众液压管道技术有限公司 | Cooling machine for wind power electricity generation current transformer |
-
2009
- 2009-12-28 CN CN 200910312442 patent/CN102107894B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN102107894B (en) | 2013-01-02 |
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| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |