CN206359468U - A kind of coke oven coke oven uprising tube waste heat boiler pressure regulating system - Google Patents
A kind of coke oven coke oven uprising tube waste heat boiler pressure regulating system Download PDFInfo
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- CN206359468U CN206359468U CN201720021129.XU CN201720021129U CN206359468U CN 206359468 U CN206359468 U CN 206359468U CN 201720021129 U CN201720021129 U CN 201720021129U CN 206359468 U CN206359468 U CN 206359468U
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- coke oven
- drum
- heat
- pressure regulating
- regulating system
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
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- Coke Industry (AREA)
Abstract
The utility model discloses a kind of coke oven coke oven uprising tube waste heat boiler pressure regulating system, it is included between the delivery port of drum and the entrance of drum and a heat recovery circuit is formed by the water route of pipeline series connection forced circulation pump, rising heat exchange of heat pipe；The venthole of the drum is communicated to steam pipe system；The system is also：The water route of external water pipe, oxygen-eliminating device/steam turbine, tank, feed pump, flue gas heat-exchanger is sequentially connected in series to the drum entrance by pipeline.The coke oven coke oven uprising tube waste heat boiler pressure regulating system that the utility model is provided, for fully reclaiming the residual heat resources in coke making process flow, it is accurate to determine actual maintenance time of origin, stablize steam water-level in repair time section regulation quantity of steam, while increasing vapour gas yield.
Description
Technical field
The utility model is related to raw coke oven gas residual neat recovering system in a kind of coke making process, more particularly to a kind of coke oven coke oven uprising tube
Waste heat boiler pressure regulating system.
Background technology
The high efficiente callbacks of the residual heat resources produced in coke making process flow is utilized, and sets up resources conservation, environment-friendly
The Main way of green coke-oven plant's energy-conservation, is also to reduce one of main path of coke oven energy consumption.Wherein, from carbonization chamber through tedge
The heat that the raw coke oven gas of 650 DEG C -700 DEG C of effusion is taken out of accounts for 35% or so of coke oven quantity of heat given up, and coal chemical enterprise is typically used
Raw gas temperature is dropped to less than 85 DEG C by the mode that ammoniacal liquor sprays in bridge tube, and substantial amounts of residual heat resources can not be utilized effectively.
Waste heat dum boiler in coking tedge residual neat recovering system technological process, steam water-level is that reaction boiler energy and working medium are flat
The key parameter of weighing apparatus, steam water-level is higher or relatively low will all have a strong impact on safe operation of the boiler.When drum pressure bust, stove water
Saturation temperature drop to pressure it is relatively low when saturation temperature, make stove water largely release heat to be evaporated, then in stove water
Steam bubble increase, steam water interface volumetric expansion promotes water level to rise quickly, forms false water level；When drum pressure jumps, then
Corresponding saturation temperature improves a part of heat and is used for heating furnace water, and is then reduced for the heat of vapourizing furnace water, in stove water
Steam bubble amount is reduced, and is made the volume contraction of steam water interface, is promoted water level to decline quickly, forms false water level.Drum false water level
There is potential safety hazard in coking tedge waste heat reclaiming process flow, easily occur dangerous accident.Due to the sensible heat of recovery
The raw coke oven gas produced all from each carbonization chamber of coke oven, and the temperature and flow of the raw coke oven gas that each carbonization chamber is produced are with each charing
The retorting time change of indoor mixed coal, the raw coke oven gas flow that destructive distillation initial stage to destructive distillation latter stage produces is more, and temperature is higher, destructive distillation
The flow and temperature for the raw coke oven gas that mid-term is produced to destructive distillation latter stage are gradually reduced.The waste coal produced to carbonization chamber during destructive distillation latter stage
Temperature degree is less than 200 DEG C, and the flow of raw coke oven gas is seldom not suitable for rising heat exchange of heat pipe recovery sensible heat.Each carbonization chamber of coke oven is done
Period of the process of mixed coal from coalingging to coke pushing is evaporated for a cycle, and all carbonization chambers of coke oven are generally divided into 2 or 5 or 9 groups,
After all carbonization chamber numberings of coke oven, the carbonization chamber group of 2 or 5 or 9, interval of numbering carbonization chamber is one group, and each group carbonization chamber is pressed
Number sorting is from as low as large cyclic operation, and per tour has the mixed coal in 1 to 2 group carbonization chamber to be in destructive distillation latter stage for 8 hours, need to push away
It is defocused to coaling again into next destructive distillation phase.Operating personnel will according to previous order of classes or grades at school coaling the time and plan destructive distillation when
Between, layout next coke pushing plan coke pushing timetable can be reserved between the carbonization chamber group in coke pushing timetable or in group
Without the repair time of pushing coke operation, the remaining plan in the carbonization chamber or group of the interior next group of plan coke pushing of repair time section
Mixed coal in the carbonization chamber of coke pushing is all in destructive distillation latter stage, and the temperature and flow of the raw coke oven gas of generation are all not enough to reclaim aobvious
Heat, so causes tedge residual neat recovering system to decline in the steam pressure that repair time section is produced, this pressure oscillation is with inspection
Repair the generation in cycle and occur so that the drum pressure and water level of repair time section tedge residual neat recovering system are unstable, shape
Into false water level, potential safety hazard is brought to tedge residual neat recovering system.But the repair time is dynamically can be with coke oven each group charcoal
The activity duration for changing room postpones or shifts to an earlier date or disappear, and the drum pressure and water level to control tedge residual neat recovering system bring tired
It is difficult.In the prior art using the positional information and the analog quantity information of the coke pusher sensor of coking vehicle for monitoring coking vehicle
To generate coke pushing time sheet in real time, the actual maintenance time of origin of identification, but during coking car inspection and repair also can maloperation cause
False coke pushing time sheet is produced, leads to not recognize actual maintenance time of origin, is unfavorable for controlling to rise with this
The drum pressure and water level of pipe residual neat recovering system.
It is necessarily required to control pollution using cleaner during coke oven coke-pusher, during coke is released, often
More high temperature paroxysmal flue dust is produced, the temperature of flue dust and the time of dedusting can be monitored simultaneously, just can generate and accurately push away
Burnt time sheet, beneficial to the actual maintenance time of origin of identification, takes technological means to control tedge waste heat in the corresponding period
The drum pressure and water level of recovery system, it is to avoid form false water level, potential safety hazard is brought to tedge residual neat recovering system.
Utility model content
The purpose of this utility model is there is provided a kind of coke oven coke oven uprising tube waste heat boiler pressure regulating system, for abundant
The residual heat resources produced in coke making process flow are reclaimed, coke oven each group carbonization chamber is recognized by sensor, it is accurate to determine actual inspection
Time of origin is repaiied, stablizes steam water-level in repair time section regulation quantity of steam, while adding vapour gas yield.
The technical solution of the utility model：A kind of coke oven coke oven uprising tube waste heat boiler pressure regulating system, is included in drum
A recuperation of heat is formed between delivery port and the entrance of drum by the water route of pipeline series connection forced circulation pump, rising heat exchange of heat pipe to return
Road；The venthole of the drum is communicated to steam pipe system；The system is also：
The water route of external water pipe, oxygen-eliminating device/steam turbine, tank, feed pump, flue gas heat-exchanger is sequentially connected in series by pipeline
To the drum entrance.
Further, also connected between drum delivery port and drum entrance the flue gas heat-exchanger water route formed one heat
Reclaim loop.
Further, the flue gas heat-exchanger includes that the flue gas road and the water route of heat exchange can be carried out；The flue gas
Road connects a blower fan.
Further, the two ends of the tank of series connection and feed pump are also returned by a pipeline connection one water circulation of formation
Road；
The tank also connects the external water pipe with moisturizing.
Further, the water route outlet of the flue gas heat-exchanger and/or the water route outlet of rising heat exchange of heat pipe are connected
Pipeline on be provided with stop valve.
Further, the water route outlet of the flue gas heat-exchanger and the rising heat exchange of heat pipe waterway inlet also pass through pipe
Road is connected.
Further, the water route outlet for rising heat exchange of heat pipe also connects an accident exhaust stack.
Further, the height of the entrance on the drum is higher than its delivery port.
Further, the coke oven coke oven uprising tube waste heat boiler pressure regulating system also includes the actual maintenance time of origin of monitoring
Sensor, the sensor includes scanner, proximity switch and thermocouple, and the installation of TC is described to connect on dust removing tube
Nearly switch leading on smoke pipe lid switching mechanism installed in coke oven operation vehicle, the scanner is arranged on coke oven operation vehicle；
The dust removing tube is provided with dust removal port, and the dust removal port is provided with dedusting turnover panel, and the dedusting turnover panel is provided with dedusting strut, institute
State dedusting strut and be provided with the mark for corresponding to carbonization chamber.
Further, the thermocouple is electrically connected with PLC servers by signal cable, the scanner, close to opening
Pass is electrically connected with wireless communication module in coke oven operation vehicle respectively, and the PLC servers are electrically connected with Industrial Control Computer.
Compared with prior art, the utility model has the advantages that：On a kind of coke oven that the utility model is provided
Riser waste heat boiler pressure regulating system, it is by the residual heat resources in absorption from flue gas heat exchanger, the water vapour after heat exchange is defeated
The steam delivered in drum, supplement drum, so that the pressure of stable drum, coke oven each group carbonization chamber is recognized by sensor, it is accurate
Actual maintenance time of origin is determined, stablizes steam water-level in repair time section regulation quantity of steam, prevents drum from occurring false
Water level, eliminates potential safety hazard, it is ensured that the stable operation of whole coke making process, while also add vapour gas yield.
Brief description of the drawings
Fig. 1 is a kind of stream for coke oven coke oven uprising tube waste heat boiler pressure regulating system preferred embodiment that the utility model is provided
Journey block diagram；
Fig. 2 is a kind of another preferred embodiment of coke oven coke oven uprising tube waste heat boiler pressure regulating system that the utility model is provided
FB(flow block)；
Fig. 3 is flue gas heat-exchanger in a kind of coke oven coke oven uprising tube waste heat boiler pressure regulating system that the utility model is provided
The structural representation of blast pipe and discharge pipe；
Fig. 4 is drum water inlet position in a kind of coke oven coke oven uprising tube waste heat boiler pressure regulating system that the utility model is provided
The structural representation put；
Fig. 5 is coke oven operation vehicle in a kind of coke oven coke oven uprising tube waste heat boiler pressure regulating system that the utility model is provided
With the structural representation of dust removing tube；
Coke-pushing Management System in a kind of coke oven coke oven uprising tube waste heat boiler pressure regulating system that Fig. 6 the utility model is provided
Structural representation.
Embodiment
The utility model is further described with reference to the accompanying drawings and examples, but is not intended as to the utility model
The foundation of limitation.
Embodiment.A kind of coke oven coke oven uprising tube waste heat boiler pressure regulating system, as shown in figure 1, including oxygen-eliminating device/steam turbine
10th, tank 20, feed pump 30, flue gas heat-exchanger 40, drum 50, forced circulation pump 60 and rising heat exchange of heat pipe 70,
External water pipe 11 is connected with the oxygen-eliminating device/steam turbine 10, and the oxygen-eliminating device/steam turbine 10 passes through the first pipeline 12
It is connected with the tank 20, the tank 20 is connected by the second pipeline 13 with the feed pump 30, the feed pump 30 passes through
3rd pipeline 14 is connected with the flue gas heat-exchanger 40, and the flue gas heat-exchanger 40 passes through the 4th pipeline 15 and the drum
50 connections, the drum 50 is connected by the 5th pipeline 16 with the forced circulation pump 60, and the forced circulation pump 60 passes through the
Six pipelines 17 are connected with least one rising heat exchange of heat pipe 70；The rising heat exchange of heat pipe 70 passes through the 7th pipeline 18 and the vapour
Bag 50 is connected, and the drum 50 is connected by the 8th pipeline 21 with steam pipe system.
Specifically, the drum 50 is set to 2, and one of them, as standby, is examined in pipeline circulation when drum is in
During repairing or when damaging, standby drum is enabled, standby drum is avoided that stopping production.
The coke oven coke oven uprising tube waste heat boiler pressure regulating system specific work process that the utility model is provided：By oxygen-eliminating device/
The temperature that steam turbine 10 comes is 80-90 DEG C of water, and being delivered to tank 20 through the first pipeline 12 accumulates, through the second pipeline 13 by
Feed pump 30 is delivered to after flue gas heat-exchanger 40, the heat of absorption from flue gas heat exchanger 40 by the 3rd pipeline 14, is formed
The mixture of 120-200 DEG C of water and steam, now, the mixture are delivered to the vapour in drum 50, drum 50 through the 4th pipeline 15
Aqueous mixtures, after gas-liquid separation, gas is delivered to steam pipe system through the 8th pipeline 21, and liquid is forced to follow through forced circulation pump 60
It is delivered to after ring by the 6th pipeline 17 after rising heat exchange of heat pipe 70, absorbs the waste heat for rising heat exchange of heat pipe 70, temperature is further carried
After rising, steam water interface in drum 50, drum 50 is delivered to again after gas-liquid separation through the 7th pipeline 18, and gas is through the
Eight pipelines 21 are delivered to steam pipe system, and liquid is continued cycling through.
In the process, the heat for rising and being produced in heat exchange of heat pipe 70 has been reclaimed, however, when coke oven is in turn(a)round,
Due to stopping aerogenesis in coke oven, then the heat being connected in the rising heat exchange of heat pipe 70 above coke oven can be reduced, then can cause vapour
False water level is easily formed in pressure transient in bag 50, the timing of the pressure instability of drum 50, drum 50, drum false water level exists
There is potential safety hazard in coke making process flow, easily occur dangerous accident, therefore, come by oxygen-eliminating device/steam turbine 10
Heat in water, absorption from flue gas heat exchanger 40, and the water vapour that temperature is increased into 120-200 DEG C is delivered to drum 50, mends
The water vapour filled in drum 50, so that the pressure of stable drum, prevents drum from false water level occur, eliminate potential safety hazard, is protected
The stable operation of whole coke making process is demonstrate,proved, while also add vapour gas yield.
As shown in Fig. 2 as another preferred embodiment of the present utility model, the drum 50 passes through the 9th pipeline 24 and institute
State flue gas heat-exchanger 40 to connect, the flue gas heat-exchanger 40 is connected by the tenth pipeline 25 with the drum 50.
Specifically, the gas-liquid mixture in drum 50 is after gas-liquid separation, and gas is delivered to steam pipe through the 8th pipeline 21
Net, liquid is then by an outlet pipe part for the bottom of drum 50 through the 5th pipeline 16, after the forced circulation of forced circulation pump 60,
By the 6th pipeline 17 be delivered to rising heat exchange of heat pipe 70 exchange heat after, temperature further lifting after, it is defeated again through the 7th pipeline 18
Drum 50 is delivered to, another part liquid continues on to flue gas heat-exchanger 40, further absorption from flue gas through the 9th pipeline 24
After the heat of heat exchanger 40, temperature is further raised, and as steam water interface, now, can be set in the tenth pipeline 25 one strong
Circulating pump processed, after forced circulation pump forced circulation, is delivered to drum 50, and this circulatory system has fully reclaimed flue gas heat exchange
The heat of device 40, adds the yield of steam, while also contributing to stablize the steam pressure in drum 50.
As shown in Figure 3, it is preferable that the flue gas heat-exchanger 40 is provided with blast pipe 41 and discharge pipe 42, the air intake
Pipe 41 is connected with blower fan 43；As shown in figure 1, the external water pipe 11 is connected by collateral pipeline 22 with first pipeline 12.
Specifically, when starting to the scheduled overhaul period, thermal medium is reduced in repair time section rising heat exchange of heat pipe, and the steam of generation subtracts
It is few, by blower fan 43, the flue gas flow increase heat exchange amount extracted out in flue gas heat-exchanger is increased, so that increase the yield of steam,
Be conducive to stablizing drum pressure, be conducive to the stable long-term operation of whole coke oven coke oven uprising tube waste heat boiler pressure regulating system.
Preferably, the 3rd pipeline 14 is connected by the 11st pipeline 23 with first pipeline 12.11st pipeline
23 as collateral branch's pipeline between tank 20 and feed pump 30, when the fluid flow increase in the pipe of the 3rd pipeline 14, the tenth
One pipeline 23 sets circulating pump, by circulating pump, partially liq is delivered into the first pipeline 12 by the 11st pipeline 23, is back to
In tank 20.11st pipeline 23 can adjust the fluid flow into flue gas heat-exchanger 40.
Preferably, the 4th pipeline 15 is provided with the first stop valve 31, and the 7th pipeline 18 is provided with the second cut-off
Valve 32.It is located between first valve 31 and the feed pump 40 on the 4th pipeline 15 and is provided with the 12nd pipeline 26,
12nd pipeline 26 is connected with the 6th pipeline 17.
Specifically, it is located between second valve 32 and the rising heat exchange of heat pipe 50 on the 7th pipeline 18 and sets
There is accident exhaust stack 19.
Specifically, the 12nd pipeline 26 is provided with the 3rd stop valve 33.When drum breaks down, the first stop valve
31 close the 4th pipeline 15, and the second stop valve 32 closes the 7th pipeline 18, will be exchanged heat by the 12nd pipeline 26 by flue gas
Steam water interface after the heat exchange of device 40, via the 6th pipeline 17 being connected with the 12nd pipeline 26, by rising heat exchange of heat pipe 70
Afterwards, directly discharged from accident exhaust stack 19, eliminate the potential safety hazard that drum failure is present.
As shown in figure 4, the height of the entrance 51 on the drum 50 is higher than its delivery port.Using this set, reduce into
Enter impact of the gas-liquid mixture to original liquid level in drum in drum, be conducive to stablizing the liquid level of drum.Meanwhile, on drum
Entrance is also connected with the 4th pipeline 15.
As shown in figure 5, the coke oven coke oven uprising tube waste heat boiler pressure regulating system also includes the actual maintenance time of origin of monitoring
Sensor, the sensor include scanner, proximity switch and thermocouple, the thermocouple 84 be arranged on dust removing tube 80 on,
The proximity switch 92 is led on smoke pipe lid switching mechanism installed in coke oven operation vehicle 90, and the scanner 91 is arranged on coke oven
On working truck 90；The dust removing tube 80 is provided with dust removal port, and the dust removal port is provided with dedusting turnover panel 81, the dedusting turnover panel
81 are provided with dedusting strut 82, and the dedusting strut 82 is provided with the mark 83 corresponding to carbonization chamber.
Specifically, dust removing tube 80 is provided with the coke side of coke oven, it is burnt when the mixed coal in coke furnace carbonization chamber is in destructive distillation latter stage
Stove working truck carries out pushing coke operation according to the coke pushing schedule plan of layout, will be arranged on coke oven operation vehicle coke guide
Lead smoke pipe and be covered in the dust removal port that dust removing tube 80 is provided with and carry out dedusting.The mark 83 can be the plate provided with Quick Response Code.
The plate of Quick Response Code is arranged on the dedusting turnover panel 81 on dust removing tube and corresponded with dust removal port, each dust removal port and each charcoal of coke oven
Change room to correspond, Quick Response Code is loaded with the heat (batch) number information of correspondence carbonization chamber.
Preferably, the thermocouple 84 and PLC servers are electrically connected with by signal cable, the scanner 91, close
Switch 92 is electrically connected with wireless communication module in coke oven operation vehicle 90 respectively, and the PLC servers are electromechanical with Industry Control
Property connection.Wherein, PLC servers connect interchanger by industrial Ethernet, are connected with interchanger by industrial Ethernet
Meet Surveillance center.
During coke oven operation vehicle coke guide operation, coke guide is moved to job position, and pusher machine is provided with dedusting push rod, removed
CCD camera and proximity switch are housed on dirt push rod, on working truck coke guide when leading smoke pipe and carrying out dedusting, dedusting push rod is extended
Before dedusting strut 82, now, CCD camera scans Quick Response Code to recognize heat (batch) number, and CCD camera can be by the switching value of dedusting push rod
Signal enabling barcode scanning, CCD camera is electrically connected with emitter, heat (batch) number is sent into ground Coke-pushing Management System, dedusting push rod is pushed away
Dynamic dedusting turnover panel 81 is to open position, and proximity switch 92 monitors the positional information of dedusting push rod, and proximity switch 92 is electrically connected with hair
Temperature sensor is housed on injection device, earthward Coke-pushing Management System emission switch amount signal, dust removing tube 80, also can riser upwards
Management system launches digital quantity signal, when temperature reaches threshold values, record operating time and heat (batch) number (point coke oven number and location number), people
On the day of work layout after operation planning, next operation meter is inputted by the tedge oven pushing management software on Industrial Control Computer
Draw, following information, 1 are included in operation planning record#、2#The operation planning of each carbonization chamber group of stove, activity duration and repair time
Section, above operation planning is each carbonization chamber numbering and pushing schedule of plan coke pushing, and the above activity duration is each in operation planning
The plan moment of carbonization chamber coke pushing, above repair time section is coke pushing interval time section or each carbonization chamber group between each carbonization chamber group
Coke pushing interval time section between the carbonization chamber and carbonization chamber of interior plan coke pushing, when starting to the scheduled overhaul period, passes through two
The identification of code operation note identifying system is tieed up, for example, 2#Whether stove, the most end position heat (batch) number of operation planning in the works on duty has been recorded
Enter operating time and heat (batch) number, if non-typing, aborting task, if typing increases the flue gas flow increase extracted out in flue gas heat-exchanger
Heat exchange amount；At the end of the scheduled overhaul period, 2 are recognized by Quick Response Code operation note identifying system#Stove in the works next
The first position number of operation planning, if typing, if non-typing, not aborting task, if typing, aborting task, if typing reduces
The flue gas flow extracted out in flue gas heat-exchanger reduces heat exchange amount；In the process, due to scanning Quick Response Code by CCD camera,
It can rapidly realize and be accurately positioned carbonization chamber heat (batch) number residing for coke guide, pass through proximity switch and detect that the position of dedusting push rod is believed
Breath, can rapidly realize the corresponding dust removal port of carbonization chamber for being accurately positioned and being ready for coke pushing operation, and temperature sensor is detected
Because of the temperature information for the high-temperature gas that dedusting is produced, confirm that the carbonization chamber for being ready for coke pushing operation there occurs that coke pushing is operated, lead to
Cross Coke-pushing Management System software analysis occur coke pushing operation carbonization chamber heat (batch) number whether the most end position heat (batch) number phase with operation planning
Together, it is or identical with the first position heat (batch) number of next operation planning, the hair of accurate acquisition repair time section can be rapidly realized with this
Raw moment or finish time.
For example：Normally for every eight hours, there are 46 stove coke pushings, 1#Stove has 23 stoves, 2#Stove has 23 stoves, per tour 1#With 2#Respectively pause is pushed away stove
Jiao's operation 4 hours, is divided to two sections of repair times, respectively about 2 hours, and thermal medium is reduced (because treating in repair time section rising heat exchange of heat pipe
Coke pushing heat (batch) number is close to coking latter stage, and every section of plan has 11 stoves to be in treat coke pushing state), the steam of generation is reduced, if can detect
The actual time started of maintenance, accurate adjustment quantity of steam can stablize steam water-level, and increase production.
As shown in fig. 6, in Coke-pushing Management System, whole system is based on the existing local area network of company, main hard
Part configuration includes：Database server 1, the client station of networking and printer are some (depending on concrete application situation
It is fixed).In view of existing physical condition, when building system application platform, by the database server in Central Control Room and therewith
A nearest client station merges into a machine, with cost-effective.
User includes two kinds of roles in system：Central Control Room operating personnel and operation area administrative staff, both authority responsibilities
It is different.Central Control Room operating personnel mainly complete the input of per tour coke pushing production schedule and pipe by client station
Reason, printing pusher machine driver blank table and coke pushing plan are distributed to related personnel to guide production, and by pusher machine driver feedback
The coke pushing record input returned is into system.In a word, Central Control Room operating personnel are to the typing of routine basis data and pipe in system
Reason serves important function, is the key that system is able to run well.And operation area administrative staff then be responsible for System Privileges distribution,
System important parameter sets (change regulation coking time) and can read production report：Including coke pushing account, daily paper and monthly magazine
Deng.Finally, operation area administrative staff can be understood coke production situation in time by analytical statement and make appropriate adjustment, be section
Learn rational production and important evidence is provided.
This Coke-pushing Management System at utmost reduces cost designing and developing, careful analysis coking life in development process
The management characteristic of production. art link and the actual conditions of coke oven, it is convenient, it is quick, accurate.At utmost mitigate after putting into operation
The duplication of labour of relevant staff, makes it be engaged in more creative work, is that enterprise creates more values.
Described above is preferred embodiment of the present utility model, can not be limited certainly with this utility model it
Interest field, it is noted that for those skilled in the art, before the utility model principle is not departed from
Put, some improvement and variation can also be made, these are improved and variation is also considered as protection domain of the present utility model.
Claims (10)
1. a kind of coke oven coke oven uprising tube waste heat boiler pressure regulating system, is included between the delivery port of drum and the entrance of drum and leads to
Cross pipeline series connection forced circulation pump, rise one heat recovery circuit of water route formation of heat exchange of heat pipe；The venthole connection of the drum
To steam pipe system；It is characterized in that：The system is also：
The water route of external water pipe, oxygen-eliminating device/steam turbine, tank, feed pump, flue gas heat-exchanger is sequentially connected in series to institute by pipeline
State drum entrance.
2. coke oven coke oven uprising tube waste heat boiler pressure regulating system according to claim 1, it is characterised in that：
Also connected between drum delivery port and drum entrance the flue gas heat-exchanger water route formed a heat recovery circuit.
3. coke oven coke oven uprising tube waste heat boiler pressure regulating system according to claim 1 or 2, it is characterised in that：The cigarette
Road gas heat exchanger includes that the flue gas road and the water route of heat exchange can be carried out；The flue gas road connects a blower fan.
4. coke oven coke oven uprising tube waste heat boiler pressure regulating system according to claim 1, it is characterised in that：
The tank of series connection and the two ends of feed pump also pass through a pipeline connection one water-flow circuit of formation；
The tank also connects the external water pipe with moisturizing.
5. coke oven coke oven uprising tube waste heat boiler pressure regulating system according to claim 3, it is characterised in that：
The water route outlet of the flue gas heat-exchanger and/or the water route of rising heat exchange of heat pipe export and are provided with connected pipeline
Stop valve.
6. coke oven coke oven uprising tube waste heat boiler pressure regulating system according to claim 5, it is characterised in that：
The water route outlet of the flue gas heat-exchanger and the rising heat exchange of heat pipe waterway inlet also pass through pipeline connection.
7. coke oven coke oven uprising tube waste heat boiler pressure regulating system according to claim 6, it is characterised in that：
The water route outlet for rising heat exchange of heat pipe also connects an accident exhaust stack.
8. the coke oven coke oven uprising tube waste heat boiler pressure regulating system according to any one of claim 1,2 or 5-7, its feature
It is：The height of entrance on the drum is higher than its delivery port.
9. coke oven coke oven uprising tube waste heat boiler pressure regulating system according to claim 8, it is characterised in that：The coke oven rises
Pipe waste heat boiler pressure regulating system also includes the sensor of the actual maintenance time of origin of monitoring, and the sensor includes scanning
Instrument, proximity switch and thermocouple, the installation of TC is on dust removing tube, and the proximity switch is arranged on coke oven operation vehicle
Lead on smoke pipe lid switching mechanism, the scanner is arranged on coke oven operation vehicle；The dust removing tube is provided with dust removal port, described
Dust removal port is provided with dedusting turnover panel, and the dedusting turnover panel is provided with dedusting strut, and the dedusting strut, which is provided with, corresponds to charing
The mark of room.
10. coke oven coke oven uprising tube waste heat boiler pressure regulating system according to claim 9, it is characterised in that：The thermoelectricity
It is even to be electrically connected with PLC servers by signal cable, the scanner, proximity switch respectively with coke oven operation vehicle wirelessly
Communication module is electrically connected with, and the PLC servers are electrically connected with Industrial Control Computer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720021129.XU CN206359468U (en) | 2017-01-09 | 2017-01-09 | A kind of coke oven coke oven uprising tube waste heat boiler pressure regulating system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720021129.XU CN206359468U (en) | 2017-01-09 | 2017-01-09 | A kind of coke oven coke oven uprising tube waste heat boiler pressure regulating system |
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| CN206359468U true CN206359468U (en) | 2017-07-28 |
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|---|---|---|---|
| CN201720021129.XU Expired - Fee Related CN206359468U (en) | 2017-01-09 | 2017-01-09 | A kind of coke oven coke oven uprising tube waste heat boiler pressure regulating system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107043631A (en) * | 2017-01-09 | 2017-08-15 | 江苏龙冶节能科技有限公司 | A kind of coke oven coke oven uprising tube waste heat boiler pressure regulating system |
| CN111996013A (en) * | 2020-09-09 | 2020-11-27 | 常州江南冶金科技有限公司 | Ascending pipe heat exchanger with internal overpressure automatic pressure relief adjusting and releasing interlocking device |
-
2017
- 2017-01-09 CN CN201720021129.XU patent/CN206359468U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107043631A (en) * | 2017-01-09 | 2017-08-15 | 江苏龙冶节能科技有限公司 | A kind of coke oven coke oven uprising tube waste heat boiler pressure regulating system |
| CN111996013A (en) * | 2020-09-09 | 2020-11-27 | 常州江南冶金科技有限公司 | Ascending pipe heat exchanger with internal overpressure automatic pressure relief adjusting and releasing interlocking device |
| CN111996013B (en) * | 2020-09-09 | 2022-04-15 | 常州江南冶金科技有限公司 | Ascending pipe heat exchanger with internal overpressure automatic pressure relief adjusting and releasing interlocking device |
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Granted publication date: 20170728 Termination date: 20220109 |