CN204022754U - For the ammoniacal liquor system of tamping coke oven dust - Google Patents
For the ammoniacal liquor system of tamping coke oven dust Download PDFInfo
- Publication number
- CN204022754U CN204022754U CN201420426241.8U CN201420426241U CN204022754U CN 204022754 U CN204022754 U CN 204022754U CN 201420426241 U CN201420426241 U CN 201420426241U CN 204022754 U CN204022754 U CN 204022754U
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- Prior art keywords
- carbonizing chamber
- water pipe
- ammonium hydroxide
- valve
- ammonia water
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- 235000011114 ammonium hydroxide Nutrition 0.000 title claims abstract description 205
- 239000000571 coke Substances 0.000 title claims abstract description 20
- 239000000428 dust Substances 0.000 title claims abstract description 16
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims abstract description 152
- 238000010000 carbonizing Methods 0.000 claims abstract description 122
- 239000000908 ammonium hydroxide Substances 0.000 claims abstract description 67
- 239000000779 smoke Substances 0.000 claims abstract description 23
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract description 15
- 239000003500 flue dust Substances 0.000 abstract description 14
- 238000004939 coking Methods 0.000 abstract description 9
- 229910021529 ammonia Inorganic materials 0.000 abstract description 7
- 239000007921 spray Substances 0.000 abstract description 7
- 235000019504 cigarettes Nutrition 0.000 abstract description 5
- 238000000034 method Methods 0.000 description 6
- 239000007789 gas Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 239000003245 coal Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000003546 flue gas Substances 0.000 description 3
- 230000008676 import Effects 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000004484 Briquette Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000009885 systemic effect Effects 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Coke Industry (AREA)
Abstract
The utility model relates to tamping coking, discloses a kind of ammoniacal liquor system for tamping coke oven dust.This system comprises ammoniacal liquor supply system and multiple carbonizing chamber, in described multiple carbonizing chamber, be connected with #N+a carbonizing chamber by smoke guiding bogie when #N carbonizing chamber is coaling, ammoniacal liquor supply system comprises the first ammonium hydroxide delivery pump, second ammonium hydroxide delivery pump, first ammonia water pipe and the second ammonia water pipe, first ammonium hydroxide delivery pump is communicated with the first ammonia water pipe, second ammonium hydroxide delivery pump is communicated with the second ammonia water pipe, each carbonizing chamber comprises I group carbonizing chamber and II group carbonizing chamber, in each carbonizing chamber | a| I group carbonizing chamber and | the interlaced arrangement of a| II group carbonizing chamber, first ammonia water pipe is communicated with I group carbonizing chamber, second ammonia water pipe is communicated with II group carbonizing chamber.I group carbonizing chamber and II group carbonizing chamber are connected to and independently supply ammoniacal liquor system within the system, thus avoid both ammonia spray fluctuations in discharge and mutually have an impact, and ensure the stability leading cigarette suction, avoid the excessive phenomenon of flue dust.
Description
Technical field
The utility model relates to tamping coking, especially a kind of ammoniacal liquor system for tamping coke oven dust.
Background technology
TAMPING COKING PROCESS is one of coking process expanding coking coal source, and tamping coke furnace is the special type of furnace of tamping coking.Affect by coal resource, tamping coke furnace is progressively favored by Ge great coke-oven plant, but the flue dust collecting of tamping coke furnace in the process of coalingging is comparatively difficult, and the dedusting method that current furnace roof generally adopts adopts U-tube smoke guiding bogie to carry out smoke prevention and dust control.The principle of work of U-tube smoke guiding bogie produces negative-pressure sucking by opening high pressure aqua ammonia high-velocity jet, and the part flue dust produced when coalingging is sucked effuser by this hole upcast; Another part flue dust is connected the coking chamber being in coking latter half importing vicinity with the smoke guiding hole of furnace roof band manhole cover by U-shaped pipe, finally import effuser.When coalingging to N# carbonizing chamber, by U-tube smoke guiding bogie, this part flue dust can be imported the carbonizing chambers such as #N+2 carbonizing chamber, N-1# carbonizing chamber or #N+4.As shown in Figure 1, when carbonizing chamber is not coaling, low pressure ammoniacal liquor is supplied by low pressure ammoniacal liquor pipeline 9, low pressure ammoniacal liquor sprays at the upcast bridge tube of carbonizing chamber, and when coalingging to #1 carbonizing chamber, smoke guiding bogie 7 is adopted to be connected with #3 carbonizing chamber by #1 carbonizing chamber, the T-valve of 1 carbonizing chamber is regulated by the oil cylinder that smoke guiding bogie is arranged, cut off low ammoniacal liquor pipeline is supplied the low pressure ammoniacal liquor of #1 carbonizing chamber, adopt high pressure aqua ammonia supply system to 1# carbonizing chamber supply high pressure aqua ammonia, high pressure aqua ammonia sprays at the upcast bridge tube of 1# carbonizing chamber, make a part coaling produce flue dust enter effuser 8 from the upcast of #1 carbonizing chamber, oil cylinder simultaneously by smoke guiding bogie is arranged regulates the T-valve of #3 carbonizing chamber, disconnected low pressure ammoniacal liquor pipeline is supplied the low pressure ammoniacal liquor of #3 carbonizing chamber, adopt high pressure aqua ammonia system to #3 carbonizing chamber supply high pressure aqua ammonia, make another part coaling produce flue dust enter #3 carbonizing chamber from #1 carbonizing chamber by smoke guiding bogie 7, finally enter effuser 8.The ejector action of high pressure aqua ammonia jet is the power source of whole coal-charging smoke transporting technique at the suction that upcast root produces.High pressure aqua ammonia course of injection more complicated, relates to the conversion of 2 energy.First be become kinetic energy by pressure energy, then become pressure energy by kinetic transformation again.High pressure aqua ammonia pressure will be directly connected to the size of jet velocity, in other words the power of jet ejector action, thus have decisive role to the size of upcast root suction and smoke effect.
Find after deliberation, along with coke oven opens the number of high pressure aqua ammonia valve and the change of ammoniacal liquor flow simultaneously, ammoniacal liquor terminal pressure can have greatly changed, and the fluctuation of high pressure aqua ammonia pressure will cause high pressure aqua ammonia spraying effect undesirable, directly affect flue dust transporting effect.Study a kind of effective stable high voltage ammonia pressures for this reason, effectively to save a kind of high pressure aqua ammonia system of the electric energy that aqueous ammonia pump of high pressure consumes necessary simultaneously.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of ammoniacal liquor system for tamping coke oven dust.This system can provide the ammoniacal liquor of stable pressure for ammonia spray terminal.
Ammoniacal liquor system for tamping coke oven dust disclosed in the utility model, comprise high pressure aqua ammonia supply system, low pressure ammoniacal liquor pipeline and be arranged in order multiple carbonizing chamber, in described multiple carbonizing chamber, be connected with #N+a carbonizing chamber by smoke guiding bogie when #N carbonizing chamber is coaling, described N is positive integer, described a is nonzero integer, described ammoniacal liquor supply system comprises the first ammonium hydroxide delivery pump, second ammonium hydroxide delivery pump, first ammonia water pipe and the second ammonia water pipe, described first ammonium hydroxide delivery pump is communicated with the first ammonia water pipe, second ammonium hydroxide delivery pump is communicated with the second ammonia water pipe, described each carbonizing chamber comprises I group carbonizing chamber and II group carbonizing chamber, in described each carbonizing chamber | a| I group carbonizing chamber and | the interlaced arrangement of a| II group carbonizing chamber, described each I group carbonizing chamber by the first T-valve respectively with the first ammonia water pipe and low pressure ammoniacal liquor pipeline communication, described each II group carbonizing chamber by the second T-valve respectively with the second ammonia water pipe and low pressure ammoniacal liquor pipeline communication, described first T-valve and the second T-valve are all controlled by the oil cylinder be arranged on smoke guiding bogie.
Preferably, the drive-motor of described first ammonium hydroxide delivery pump and the second ammonium hydroxide delivery pump is variable-frequency motor, and described first ammonium hydroxide delivery pump is all connected with coaling operation controller with the drive-motor of the second ammonium hydroxide delivery pump.
Preferably, described first ammonia water pipe is connected with the first safety valve, described second ammonia water pipe is connected with the second safety valve.
Preferably, this ammoniacal liquor Operation system setting has the first ammonium hydroxide delivery pump for subsequent use and the second ammonium hydroxide delivery pump for subsequent use, described first ammonium hydroxide delivery pump for subsequent use is connected with the first ammonia water pipe by the first stand-by pump valve, described second ammonium hydroxide delivery pump for subsequent use is connected with the second ammonia water pipe by the second stand-by pump valve, the ammoniacal liquor output port place of described first ammonium hydroxide delivery pump is provided with the first main pump valve, and the ammoniacal liquor output port place of described second ammonium hydroxide delivery pump is provided with the second main pump valve.
Preferably, communicating valve is connected with between described first ammonia water pipe and the second ammonia water pipe.
Preferably, be connected with coaling operation controller respectively with the oil cylinder of the second T-valve for controlling the first T-valve.
Preferably, between described first T-valve and the first ammonia water pipe, be provided with the first ball valve, between described second T-valve and the second ammonia water pipe, be provided with the second ball valve.
The beneficial effects of the utility model are: within the system, the flue dust that I group carbonizing chamber is coaling can import II group carbonizing chamber by smoke guiding bogie, and the flue dust that II group carbonizing chamber is coaling can be imported into I group carbonizing chamber, and the first ammonia water pipe is communicated with I group carbonizing chamber, second ammonia water pipe and II group carbonizing chamber, I group carbonizing chamber and II group carbonizing chamber have independently system supply high pressure aqua ammonia respectively, so, the spray of both ammoniacal liquor can not influence each other, when making coaling operation, high pressure aqua ammonia supply is stablized, thus avoids and produce the excessive phenomenon of flue dust because leading the fluctuation of cigarette suction.
Accompanying drawing explanation
Fig. 1 is the dedusting schematic diagram of #1 carbonizing chamber when coalingging;
Fig. 2 is schematic diagram of the present utility model.
Reference numeral: 1-first ammonium hydroxide delivery pump, 101-first ammonia water pipe, 102-first safety valve, 103-the first ammonium hydroxide delivery pump for subsequent use, 104-first main pump valve, 105-first stand-by pump valve, 106-first T-valve, 107-first ball valve, 2-second ammonium hydroxide delivery pump, 201-second ammonia water pipe, 202-second safety valve, 203-the second ammonium hydroxide delivery pump for subsequent use, 204-second main pump valve, 205-second stand-by pump valve, 206-second T-valve, 206-second ball valve, 3-coaling operation controller, 4-communicating valve, 5-I group carbonizing chamber, 6-II group carbonizing chamber, 7-smoke guiding bogie, 8-effuser.
In Fig. 1, arrow represents the flow direction of the flue gas produced of coalingging;
In Fig. 2, arrow represents the throughput direction of ammoniacal liquor.
Embodiment
Below in conjunction with accompanying drawing, the utility model is further illustrated.
As shown in Figure 1, the disclosed ammoniacal liquor system for tamping coke oven dust of the utility model, comprise high pressure aqua ammonia supply system, low pressure ammoniacal liquor pipeline 9 and be arranged in order multiple carbonizing chamber, in described multiple carbonizing chamber, be connected with #N+a carbonizing chamber by smoke guiding bogie when #N carbonizing chamber is coaling, described N is positive integer, described a is nonzero integer, it is characterized in that: described ammoniacal liquor supply system comprises the first ammonium hydroxide delivery pump 1, second ammonium hydroxide delivery pump 2, first ammonia water pipe 101 and the second ammonia water pipe 201, described first ammonium hydroxide delivery pump 1 is communicated with the first ammonia water pipe 101, second ammonium hydroxide delivery pump 2 is communicated with the second ammonia water pipe 201, described each carbonizing chamber comprises I group carbonizing chamber 5 and II group carbonizing chamber 6, in described each carbonizing chamber | a| I group carbonizing chamber 5 and | the interlaced arrangement of a| II group carbonizing chamber 6, described each I group carbonizing chamber 5 is communicated with the first ammonia water pipe 101 and low pressure ammoniacal liquor pipeline 9 respectively by the first T-valve 106, described each II group carbonizing chamber 6 is communicated with the second ammonia water pipe 201 and low pressure ammoniacal liquor pipeline 9 respectively by the second T-valve 206, described first T-valve 106 and the second T-valve 106 are all controlled by the oil cylinder be arranged on smoke guiding bogie.
Wherein, the value of a can make-1, 2, 4 etc., as long as when #N carbonizing chamber is coaling, #N+a carbonizing chamber is in the coking later stage, and | a| represents the absolute value of a, be connected with #N+a carbonizing chamber by smoke guiding bogie when #N carbonizing chamber is coaling, the flue dust produced of being coaling by #N carbonizing chamber imports #N+a carbonizing chamber, and because in each carbonizing chamber | a| I group carbonizing chamber 5 and | the interlaced arrangement of a| II group carbonizing chamber 6, so when #N carbonizing chamber is I group carbonizing chamber 5, #N+a carbonizing chamber must be II group carbonizing chamber 6, and when #N carbonizing chamber is II group carbonizing chamber 6, #N+a carbonizing chamber must be I group carbonizing chamber 5, that is, to I group carbonizing chamber 5 coaling produce flue gas be imported into II group carbonizing chamber 6 by smoke guiding bogie 7, and to II group carbonizing chamber 6 coaling produce flue gas be imported into I group carbonizing chamber 5 by smoke guiding bogie 7.Such as, shown in Fig. 2, N carbonizing chamber flue dust is imported the ammoniacal liquor system layout of N+2 carbonizing chamber, in figure, tamping coke furnace has carbonizing chamber #1, #2, #3, #4, #5, #6, #7, #8, #9, #10 ... I group carbonizing chamber 5 can be #3, #4, #7, #8 ... they are all connected with the first ammonia water pipe 101, now, II group carbonizing chamber 6 is #1, #2, #5, #6, #9, #10 ... they are connected with the second ammonia water pipe 201; Certain I group carbonizing chamber 5 can be #1, #4, #5, #8, #9 ..., so now, #2, #3, #6, #7, #10, #11 ... be II group carbonizing chamber 6.
And when a gets-1, I group carbonizing chamber 5 and II group carbonizing chamber 6 are be numbered the carbonizing chamber of odd number and be numbered the carbonizing chamber of even numbers respectively.
I group carbonizing chamber 5 is supplied separate with the high pressure aqua ammonia of II group carbonizing chamber 6, and both when coalingging, have phase mutual conductance cigarette, that is, the carbonizing chamber of coalingging and be now be separate all the time for leading the high pressure aqua ammonia supply of the carbonizing chamber of cigarette, thus can not have an impact mutually.
In the prior art, because each carbonizing chamber is coaling, interval time is shorter, for ensureing to supply ammoniacal liquor in time when coalingging, ammonium hydroxide delivery pump is in continuous constant pressure running status all the time, this just causes the waste of electric energy, for addressing this problem, as optimal way, the drive-motor of described first ammonium hydroxide delivery pump 1 and the second ammonium hydroxide delivery pump 2 is variable-frequency motor, and described first ammonium hydroxide delivery pump 1 is all connected with coaling operation controller 3 with the drive-motor of the second ammonium hydroxide delivery pump 2.
Under the control of coaling operation controller 3, when non-coaling operation, the first ammonium hydroxide delivery pump 1 and the second ammonium hydroxide delivery pump 2 is made to be in low-speed run state, thus saves energy, also protect the stability of pump machine envelope simultaneously.And when coaling operation, making the first ammonium hydroxide delivery pump 1 and the second ammonium hydroxide delivery pump 2 be in high-speed cruising state, its pressure-controlling is as the criterion being in micro-vacuum state with the coal port flue dust of the carbonizing chamber of coalingging.So, just power consumption can greatly have been saved.
For preventing the first ammonia water pipe 1 and the second ammonia water pipe 2 from having an accident because ammonia pressures is excessive, as optimal way, described first ammonia water pipe 101 being connected with the first safety valve 102, described second ammonia water pipe 201 is connected with the second safety valve 202.
Safety valve is a kind of safeguard protection valve; its opening and closing element is in normally off by under External Force Acting; when the pressure medium in equipment or pipeline raises, automatically open when exceeding prescribed value, exceed specified value by preventing pressure medium in pipeline or equipment to discharge medium outside system.After being provided with safety valve, just can guarantee that the ammonia pressures of the first ammonia water pipe 101 and the second ammonia water pipe 201 is all the time within security value (s).
Because ammonium hydroxide delivery pump is in continuous running status, so easily break down, if ammonium hydroxide delivery pump breaks down, then can cause ammoniacal liquor systemic breakdown, for addressing this problem, as optimal way, this high pressure aqua ammonia Operation system setting for tamping coke oven dust has the first ammonium hydroxide delivery pump 103 for subsequent use and the second ammonium hydroxide delivery pump 203 for subsequent use, described first ammonium hydroxide delivery pump 103 for subsequent use is connected with the first ammonia water pipe 101 by the first stand-by pump valve 105, described second ammonium hydroxide delivery pump 203 for subsequent use is connected with the second ammonia water pipe 201 by the second stand-by pump valve 205, the ammoniacal liquor output port place of described first ammonium hydroxide delivery pump 1 is provided with the first main pump valve 104, the ammoniacal liquor output port place of described second ammonium hydroxide delivery pump 2 is provided with the second main pump valve 204.
When the first ammonium hydroxide delivery pump 1 breaks down, just can close the first main pump valve 104, open the first stand-by pump valve 105, the first ammonium hydroxide delivery pump 103 for subsequent use is made to replace the first ammonium hydroxide delivery pump 1 to work, equally, when the second ammonium hydroxide delivery pump 2 has fault, then the second main pump valve 204 can be closed, open the second stand-by pump valve 205, make the second ammonium hydroxide delivery pump 203 for subsequent use replace the second ammonium hydroxide delivery pump 2 to work.
And be the situation that the stand-by pump solving main pump and this main pump all goes wrong, as optimal way, between described first ammonia water pipe 101 and the second ammonia water pipe 201, be connected with communicating valve 4.
Such as, when the first ammonium hydroxide delivery pump 1 and the first ammonium hydroxide delivery pump 103 for subsequent use all break down, then communicating valve can be opened, close the first main pump valve 104 and the first stand-by pump valve 105, use the second ammonium hydroxide delivery pump 2 to supply ammoniacal liquor to the first ammonia water pipe 101 and the second ammonia water pipe 201 simultaneously, although, so there will be the fluctuation of ammonia spray terminal pressure, in case of emergency can use reluctantly.By arranging ammonium hydroxide delivery pump for subsequent use and communicating valve 4 can provide double insurance for ammonia spray, race against time to greatest extent for repair provides.
In addition, because coaling in process, raw gas generation increases along with the amount increase entering carbonizing chamber of briquette, if open high pressure aqua ammonia too early, certainly will absorb large quantity of air like this enters raw gas system, causes oxygen content of crude gas to increase, and affects subsequent production.For addressing this problem, as optimal way, be connected with coaling operation controller 3 respectively with the oil cylinder of the second T-valve 106 for controlling the first T-valve 106.
So, accurately can control the first T-valve 106 and the second T-valve 206 opening/closing time by coaling operation controller 3, thus prevent from opening high pressure aqua ammonia too early, suck a large amount of outside air.During concrete control, the T-valve opening time of carbonizing chamber of coalingging is more adjacent leads the T-valve opening time of cigarette carbonizing chamber early, and the concrete opening time of high pressure aqua ammonia is in micro-vacuum state with carbonizing chamber mouth and is as the criterion.This avoid raw gas system oxygen level to exceed standard.
For convenience of maintenance, as optimal way, between described first T-valve 106 and the first ammonia water pipe 101, be provided with the first ball valve 107, between described second T-valve 206 and the second ammonia water pipe 201, be provided with the second ball valve 207.When normally running, the first ball valve 107 and the second ball valve 207 are all in normally open, and if ammoniacal liquor system malfunctions, then they can be closed, thus convenient maintenance.
Claims (7)
1. for the ammoniacal liquor system of tamping coke oven dust, comprise high pressure aqua ammonia supply system, low pressure ammoniacal liquor pipeline (9) and be arranged in order multiple carbonizing chamber, in described multiple carbonizing chamber, be connected with #N+a carbonizing chamber by smoke guiding bogie when #N carbonizing chamber is coaling, described N is positive integer, described a is nonzero integer, it is characterized in that: described ammoniacal liquor supply system comprises the first ammonium hydroxide delivery pump (1), second ammonium hydroxide delivery pump (2), first ammonia water pipe (101) and the second ammonia water pipe (201), described first ammonium hydroxide delivery pump (1) is communicated with the first ammonia water pipe (101), second ammonium hydroxide delivery pump (2) is communicated with the second ammonia water pipe (201), described each carbonizing chamber comprises I group carbonizing chamber (5) and II group carbonizing chamber (6), in described each carbonizing chamber | a| I group carbonizing chamber (5) and | the interlaced arrangement of a| II group carbonizing chamber (6), described each I group carbonizing chamber (5) is communicated with the first ammonia water pipe (101) and low pressure ammoniacal liquor pipeline (9) respectively by the first T-valve (106), described each II group carbonizing chamber (6) is communicated with the second ammonia water pipe (201) and low pressure ammoniacal liquor pipeline (9) respectively by the second T-valve (206), described first T-valve (106) and the second T-valve (106) are all controlled by the oil cylinder be arranged on smoke guiding bogie.
2. as claimed in claim 1 for the ammoniacal liquor system of tamping coke oven dust, it is characterized in that: the drive-motor of described first ammonium hydroxide delivery pump (1) and the second ammonium hydroxide delivery pump (2) is variable-frequency motor, described first ammonium hydroxide delivery pump (1) is all connected with coaling operation controller (3) with the drive-motor of the second ammonium hydroxide delivery pump (2).
3. as claimed in claim 1 for the ammoniacal liquor system of tamping coke oven dust, it is characterized in that: described first ammonia water pipe (101) is connected with the first safety valve (102), described second ammonia water pipe (201) is connected with the second safety valve (202).
4. as claim 1, the ammoniacal liquor system for tamping coke oven dust described in 2 or 3, it is characterized in that: be provided with the first ammonium hydroxide delivery pump (103) for subsequent use and the second ammonium hydroxide delivery pump for subsequent use (203), described first ammonium hydroxide delivery pump (103) for subsequent use is connected with the first ammonia water pipe (101) by the first stand-by pump valve (105), described second ammonium hydroxide delivery pump (203) for subsequent use is connected with the second ammonia water pipe (201) by the second stand-by pump valve (205), the ammoniacal liquor output port place of described first ammonium hydroxide delivery pump (1) is provided with the first main pump valve (104), the ammoniacal liquor output port place of described second ammonium hydroxide delivery pump (2) is provided with the second main pump valve (204).
5., as claimed in claim 4 for the ammoniacal liquor system of tamping coke oven dust, it is characterized in that: between described first ammonia water pipe (101) and the second ammonia water pipe (201), be connected with communicating valve (4).
6., as claimed in claim 2 for the ammoniacal liquor system of tamping coke oven dust, it is characterized in that: be connected with coaling operation controller (3) respectively with the oil cylinder of the second T-valve (106) for controlling the first T-valve (106).
7. as claimed in claim 1 for the ammoniacal liquor system of tamping coke oven dust, it is characterized in that: between described first T-valve (106) and the first ammonia water pipe (101), be provided with the first ball valve (107), between described second T-valve (206) and the second ammonia water pipe (201), be provided with the second ball valve (207).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420426241.8U CN204022754U (en) | 2014-07-30 | 2014-07-30 | For the ammoniacal liquor system of tamping coke oven dust |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420426241.8U CN204022754U (en) | 2014-07-30 | 2014-07-30 | For the ammoniacal liquor system of tamping coke oven dust |
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| CN204022754U true CN204022754U (en) | 2014-12-17 |
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| CN201420426241.8U Active CN204022754U (en) | 2014-07-30 | 2014-07-30 | For the ammoniacal liquor system of tamping coke oven dust |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109111959A (en) * | 2018-10-23 | 2019-01-01 | 马鞍山钢铁股份有限公司 | A kind of coal oven dithio-gas ammonium hydroxide cooling system |
| CN111621307A (en) * | 2020-06-04 | 2020-09-04 | 李天祥 | Smoke guide control valve and fixed smoke guide system for large coke oven |
| CN115449382A (en) * | 2022-07-29 | 2022-12-09 | 攀钢集团西昌钢钒有限公司 | SCP machine visual smokeless coal charging method and system |
-
2014
- 2014-07-30 CN CN201420426241.8U patent/CN204022754U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109111959A (en) * | 2018-10-23 | 2019-01-01 | 马鞍山钢铁股份有限公司 | A kind of coal oven dithio-gas ammonium hydroxide cooling system |
| CN109111959B (en) * | 2018-10-23 | 2024-05-03 | 马鞍山钢铁股份有限公司 | Coke oven raw gas ammonia water cooling system |
| CN111621307A (en) * | 2020-06-04 | 2020-09-04 | 李天祥 | Smoke guide control valve and fixed smoke guide system for large coke oven |
| CN115449382A (en) * | 2022-07-29 | 2022-12-09 | 攀钢集团西昌钢钒有限公司 | SCP machine visual smokeless coal charging method and system |
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