CN108059963A - A kind of energy conservation and environmental protection coking equipment - Google Patents
A kind of energy conservation and environmental protection coking equipment Download PDFInfo
- Publication number
- CN108059963A CN108059963A CN201711472579.1A CN201711472579A CN108059963A CN 108059963 A CN108059963 A CN 108059963A CN 201711472579 A CN201711472579 A CN 201711472579A CN 108059963 A CN108059963 A CN 108059963A
- Authority
- CN
- China
- Prior art keywords
- coking
- exhaust
- heat exchanger
- waste gas
- fresh air
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B27/00—Arrangements for withdrawal of the distillation gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/06—Spray cleaning
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/60—Combinations of devices covered by groups B01D46/00 and B01D47/00
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B29/00—Other details of coke ovens
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B45/00—Other details
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/20—Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/18—Nature of the water, waste water, sewage or sludge to be treated from the purification of gaseous effluents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Industrial Gases (AREA)
Abstract
A kind of energy conservation and environmental protection coking equipment of this reality disclosure of the invention, the coking equipment includes coke oven exhaust gas chimney, coking furnace shaft, it further includes high-temp waste gas recover, aspirating air pipe, exhaust fan, air collector, baking oven, exhaust gas distributes flow path, fresh air pipe, the high-temp waste gas recover for absorbing exhaust gas is arranged on coke oven exhaust gas chimney, aspirating air pipe one end connects high-temp waste gas recover, exhaust fan is arranged on aspirating air pipe, the exhaust outlet of baking oven is connected to the benefit wind heat exchanger entrance of coking furnace shaft through exhaust gas distribution flow path, fresh air is provided the benefit wind heat exchanger entrance for entering coking furnace shaft into wind-power by fresh air exhaust fan by the fresh air air inlet of fresh air pipe, it is connected between high-temp waste gas recover and chimney for non-tight.Coking equipment in the present invention is simple in structure, repacking is convenient, cheap, waste gas circulation is fully burnt, and environment protection standard effect is good, the saving energy, easy to spread.
Description
Technical field
The present invention relates to a kind of coking environmental protecting device technical fields, are specially a kind of energy conservation and environmental protection coking equipment.
Background technology
Coking refers to that raw coal high-temperature retorting in the case where completely cutting off air conditions is heated to 1000 DEG C or so, passes through thermal decomposition and coking
Generate the technical process of coke, coke-stove gas and coking chemistry product.Smelter coke phosphorus content is high, and the porosity is high, and intensity is big(It is special
It is not elevated temperature strength), it is the important fuel of blast furnace ironmaking and the proppant and raising agent of reducing agent and entire blast furnace stock column.
The coke-stove gas calorific capacity of coking by-product is high, is the excellent gas fuel of open hearth and heating furnace, is weight in integrated iron and steel works
The energy component wanted.Coking chemistry product is important industrial chemicals.Therefore coking production is a weight of modern steel industry
Want link.
As the industry of domestic and world steel is grown rapidly, the demand sharp increase to coking product, investment rises gradually day
Temperature, industry production capacity are expanded rapidly, but coking industry resource consumption is high, and production discharge is big, particularly harmful substance in emission
It is more, the serious wasting of resources and environmental pollution are caused, immense pressure is brought to national economy sustainable health development, so as to also hinder
The fast development of coking industry is hindered.
In traditional coking process, coke-stove gas generates high-temp waste gas by flue, accumulation of heat after burning in the combustion chamber
Room, after the part Exposure degree of exhaust gas, is directly discharged to by chimney in air by checker brick after a series of flues, these are high
The direct discharge of wet body causes environment destruction, accelerates greenhouse effects, at the same these high-temp waste gas contained it is a large amount of
Thermal energy also by wasting in vain.
A kind of transverse pipe initial cooler cooled down to coke-stove gas disclosed in Chinese patent 200710051923.X, bag
Primary cooler housing is included, epimere spray is fixed in housing and shines pipe and is sprayed with hypomere and shines pipe, is sprayed in hypomere and is provided with disconnected tower above solarization pipe
Disk controls the condensate liquid of primary cooler epimere and spray to shine liquid and directly led out without the hypomere of primary cooler, spray is avoided to shine liquid and cold
Lime set flows through primary cooler hypomere and absorbs the cold of hypomere heat exchanger tube, mitigates the thermic load of primary cooler low-temperature zone, and reduces simultaneously
The dosage of water at low temperature to reduce cost consumption, improves heat exchange efficiency of the heat exchanger tube to coal gas.But coke-stove gas heat is still
It is not effectively recycled and is utilized, while need to consume substantial amounts of cooling medium.
Chinese patent CN102478232A discloses a kind of recoverying and utilizing method of coke oven flue heat energy from waste gas, and this method is
Bypass flue by flue collector is set, heat pipe evaporator and air-introduced machine be installed successively on bypass flue, heat pipe evaporator is by coke
Fume afterheat in stove stack gases absorbs to heat cold medium, is allowed to ebullition, gasification and generates steam, for producing or living,
Exhaust gas after recovery waste heat leads back flue collector by air-introduced machine, is sent into chimney and is discharged in air.The system rate of recovery is low, structure is multiple
Miscellaneous, performance difficulty.
It is unable to that continuous production coke, environmental pollution be larger, thermal energy cannot cycle profit since traditional coke oven for iron exists
With, maintenance cost is high the defects of, therefore, be badly in need of it is a kind of it is simple in structure, can efficient circulation using coke oven exhaust gas energy conservation and environmental protection refine
Burnt equipment.
The content of the invention
The purpose of the present invention is in view of the deficiencies of the prior art and provide it is a kind of it is simple in structure, repacking is convenient, cheap,
Waste gas circulation is fully burnt, and environment protection standard effect is good, saves the energy conservation and environmental protection coking equipment of the energy.
To achieve the above object, the present invention provides following technical solution:A kind of energy conservation and environmental protection coking equipment, gives up including coke oven
Gas chimney, coking furnace shaft, it is characterised in that:It further includes high-temp waste gas recover, aspirating air pipe, exhaust fan, air collector, baking
Case, exhaust gas distribution flow path, fresh air pipe, the high-temp waste gas recover for absorbing exhaust gas are arranged on coke oven exhaust gas chimney, inhale
Feed channel one end connects high-temp waste gas recover, and exhaust fan is arranged on aspirating air pipe, for high-temp waste gas is made to enter aspirating air pipe
Suction, other end connection air collector one end of aspirating air pipe are provided, high-temp waste gas is sucked gas collection by exhaust fan by aspirating air pipe
In tank, the air inlet of the other end connection baking oven of air collector, the exhaust outlet of baking oven is connected to coking furnace shaft through exhaust gas distribution flow path
Benefit wind heat exchanger entrance, fresh air provides by the fresh air air inlet of fresh air pipe by fresh air exhaust fan
Enter the benefit wind heat exchanger entrance of coking furnace shaft into wind-power, connected between high-temp waste gas recover and chimney for non-tight.
Preferably, spaced apart filtering baffling device is equipped in the air collector, is provided on the filtering baffling device
Hole or seam.
Preferably, settler is further included, which is arranged between filtering baffling device, the filtering-depositing device
Including spray head, the bottom of air collector is provided with recycling precipitate pond.
Preferably, distributed in exhaust gas between flow path and combustion chamber and be provided with regulating valve.
Preferably, heating by the exhaust gases heat exchanger, fresh air preheating heat exchanger are further included, one end of coking furnace shaft combustion chamber is set
There are combustion head, the other end to be equipped with and mend wind heat exchanger, mend wind heat exchanger and be equipped with heating by the exhaust gases heat exchanger, heating by the exhaust gases heat exchanger one
Side connects combuster by flue, opposite side is connected to baking oven by exhaust fan, mends on wind heat exchanger by mending wind preheating machine
It is connected with fresh air air inlet.
Preferably, the combustion head is equipped with raw coal inlet, combustion fan, and combustion fan provides more oxygen and ensures day
Right gas fully burns.
Preferably, several exhaust fans are connected between the baking oven and benefit wind-heat exchanger.
Preferably, it is provided with the non-woven fabrics filtration core for absorbing large dust particle on the filtering baffling device.
Preferably, the coking wastewater after spray head settles is by reconciling pond, oil removing, dephenolize, ammonia still process biochemical treatment, finally
Discharge of wastewater after obtaining the waste water after deep purifying or will be up to standard, and can pass through tar to tar ammonia in oil removing link
Separator can will obtain sodium phenolate in dephenolize link or phenol is exquisite, can also pass through tar to tar ammonia separation steaming phenol link
Device.
Compared with prior art, beneficial effects of the present invention are as follows:
1st, the present invention is by setting the high-temp waste gas recover of absorption exhaust gas to be arranged on coke oven exhaust gas chimney, aspirating air pipe one end
High-temp waste gas recover is connected, exhaust fan is arranged on aspirating air pipe, aspirating air pipe connection air collector, air collector connection baking oven,
Baking oven connection exhaust gas distributes flow path and then is connected to the benefit wind heat exchanger entrance of coking furnace shaft, and fresh air passes through fresh air tube
The fresh air air inlet in road is provided the benefit wind heat exchanger entrance for entering coking furnace shaft into wind-power by fresh air exhaust fan, high
Connected between warm waste gas recovery device and chimney for non-tight, due to fresh air fill into and the circulating combustion of exhaust gas improve it is useless
The efficiency of combustion of gas reduces the pollution to environment, avoids the waste of high-temp waste gas.
2nd, the energy conservation and environmental protection coking equipment that sets of the present invention is simple in structure, repacking is convenient.
3rd, the present invention can reduce the big pollutant of wind speed and filtering of high-temp waste gas by setting filtering baffling device, if
Recycling can be precipitated by the bulky grains such as tar, dust object by putting spray head.
4th, the present invention significantly can reduce the waste of energy consumption using the heat of original pipeline, improve energy utilization rate, drop
The temperature of low outer waste air reduces production cost.
Description of the drawings
Fig. 1 handles schematic diagram for a kind of existing high-temp waste gas;
Fig. 2 is the schematic diagram that the coke oven combustion gas circulating combustion of the present invention utilizes;
Fig. 3 is the schematic diagram of Treatment of Coking Effluent of the present invention after spray head sprays;
In Fig. 2-3:1 coking by coke oven high-temp waste gas, 2 spray columns, 3 filters, 4 high energy photodissociation, 5 exhaust fans, 6 exhaust pipes, 7 cokes
Wind heat exchanger, 9 coke oven exhaust gas chimneys, 10 high-temp waste gas recovers, 11 aspirating air pipes, 12 exhaust fans, 13 filterings are mended in furnace body, 8
Isolating device, 14 spray heads, 15 air collectors, 16 combustion chambers, 17 qi leel dispensing line, 18 regulating valves, 19 fresh air pipes, 20 are taken out
Pond, 23 oil removings, 24 dephenolizes, 25 ammonia still processs, 26 tar to tar ammonia water separator, 27 ammonia steam are reconciled in wind turbine, 21 coking wastewaters, 22
To sulphur ammonia or ammonolysis craft, 28 biochemical treatments, 29 deep purifyings, 30 it is up to standard after waste water.
Specific embodiment
Below in conjunction with the attached drawing in the embodiment of the present invention, the technical solution in the embodiment of the present invention is carried out clear, complete
Site preparation describes, it is clear that described embodiment is only part of the embodiment of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, those of ordinary skill in the art are obtained every other without making creative work
Embodiment belongs to the scope of protection of the invention.
Embodiment 1
It please refers to Fig.1, existing coking by coke oven high-temp waste gas 1 is after the spray of spray column 2 and then using filter 3
Filtration filters off large particulate matter, then by the photolysis of high energy photodissociation 4, finally will meet discharge by exhaust fan 5
The gas of standard is discharged to by exhaust pipe 6 in air, and such mode wastes high energy resource, and cannot recycle high energy exhaust gas.
Referring to Fig. 2, a kind of energy conservation and environmental protection coking equipment according to the present invention, including coke oven exhaust gas chimney 9, coking furnace shaft
7, it further includes high-temp waste gas recover 10, aspirating air pipe 11, exhaust fan 12, air collector 15, baking oven 16, exhaust gas distribution flow path
17th, fresh air pipe 19, the high-temp waste gas recover 10 for absorbing exhaust gas are arranged on coke oven exhaust gas chimney 9, aspirating air pipe 11
One end connection high-temp waste gas recover 10, exhaust fan 12 is arranged on aspirating air pipe 11, for high-temp waste gas is made to enter aspirating air pipe
11 provide suction, 15 one end of other end connection air collector of aspirating air pipe 11, and high-temp waste gas is passed through aspirating air pipe by exhaust fan 12
In 11 sucking air collectors 15, the air inlet of the other end connection baking oven 16 of air collector 15, the exhaust outlet of baking oven 16 is distributed through exhaust gas
Flow path 17 is connected to the benefit wind heat exchanger entrance 8 of coking furnace shaft 7, fresh air by fresh air pipe 19 fresh air into
Air port is provided 8 entrance of benefit wind heat exchanger for entering coking furnace shaft 7 into wind-power, high-temp waste gas recycling by fresh air exhaust fan 20
It is connected between device 10 and chimney 9 for non-tight.Spaced apart filtering baffling device 13, filtering barrier are equipped in air collector 15
Hole or seam are provided on device 13, is additionally provided with settler between filtering isolating device 13, which includes spray
Leaching first 14, recycling precipitate pond is provided in the bottom of air collector 15, is distributed between flow path 17 and combustion chamber 6 and is provided in exhaust gas
Regulating valve 18.
Embodiment 2
Referring to Fig. 2, a kind of energy conservation and environmental protection coking equipment, including coke oven exhaust gas chimney 9, coking furnace shaft 7, it further includes high temperature and gives up
Gas recover 10, aspirating air pipe 11, exhaust fan 12, air collector 15, baking oven 16, exhaust gas distribution flow path 17, fresh air pipe
19, the high-temp waste gas recover 10 for absorbing exhaust gas is arranged on coke oven exhaust gas chimney 9,11 one end of aspirating air pipe connection high-temp waste gas
Recover 10, exhaust fan 12 are arranged on aspirating air pipe 11, and suction, air intake duct are provided for high-temp waste gas is made to enter aspirating air pipe 11
15 one end of other end connection air collector in road 11, exhaust fan 12 suck high-temp waste gas in air collector 15 by aspirating air pipe 11,
The air inlet of the other end connection baking oven 16 of air collector 15, the exhaust outlet of baking oven 16 are connected to coke oven stove through exhaust gas distribution flow path 17
The benefit wind heat exchanger entrance 8 of body 7, fresh air is by the fresh air air inlet of fresh air pipe 19 by fresh air exhausting
Machine 20 provides 8 entrance of benefit wind heat exchanger for entering coking furnace shaft 7 into wind-power, is between high-temp waste gas recover 10 and chimney 9
Non-tight connects.Spaced apart filtering baffling device 13 is equipped in air collector 15, hole is provided on the filtering baffling device 13
Or stitch, settler is additionally provided between filtering isolating device 13, which includes spray head 14, in air collector 15
Bottom be provided with recycling precipitate pond, distributed in exhaust gas between flow path 17 and combustion chamber 6 and be provided with regulating valve 18.
Present invention additionally comprises heating by the exhaust gases heat exchanger, fresh air preheating heat exchanger, one end of coking furnace shaft combustion chamber is set
There are combustion head, the other end to be equipped with and mend wind heat exchanger 8,8 are equipped with heating by the exhaust gases heat exchanger, heating by the exhaust gases heat exchanger on benefit wind heat exchanger
One side connects combuster by flue, opposite side is connected to baking oven by exhaust fan, mends and is preheated on wind heat exchanger by mending wind
Machine is connected with fresh air air inlet, and combustion head is equipped with raw coal inlet, combustion fan, and combustion fan provides more oxygen and protects
Card natural gas fully burns, and several exhaust fans, filtering of the invention barrier dress are connected between baking oven 16 and benefit wind-heat exchanger 8
Put the non-woven fabrics filtration core for being provided with and absorbing large dust particle.
Embodiment 3
Fig. 2-3 are referred to, a kind of energy conservation and environmental protection coking equipment, including coke oven exhaust gas chimney 9, coking furnace shaft 7, it further includes high temperature
Waste gas recovery device 10, aspirating air pipe 11, exhaust fan 12, air collector 15, baking oven 16, exhaust gas distribution flow path 17, fresh air pipe
19, the high-temp waste gas recover 10 for absorbing exhaust gas is arranged on coke oven exhaust gas chimney 9,11 one end of aspirating air pipe connection high-temp waste gas
Recover 10, exhaust fan 12 are arranged on aspirating air pipe 11, and suction, air intake duct are provided for high-temp waste gas is made to enter aspirating air pipe 11
15 one end of other end connection air collector in road 11, exhaust fan 12 suck high-temp waste gas in air collector 15 by aspirating air pipe 11,
The air inlet of the other end connection baking oven 16 of air collector 15, the exhaust outlet of baking oven 16 are connected to coke oven stove through exhaust gas distribution flow path 17
The benefit wind heat exchanger entrance 8 of body 7, fresh air is by the fresh air air inlet of fresh air pipe 19 by fresh air exhausting
Machine 20 provides 8 entrance of benefit wind heat exchanger for entering coking furnace shaft 7 into wind-power, is between high-temp waste gas recover 10 and chimney 9
Non-tight connects.Spaced apart filtering baffling device 13 is equipped in air collector 15, hole is provided on the filtering baffling device 13
Or stitch, settler is additionally provided between filtering isolating device 13, which includes spray head 14, in air collector 15
Bottom be provided with recycling precipitate pond, distributed in exhaust gas between flow path 17 and combustion chamber 6 and be provided with regulating valve 18.
Present invention additionally comprises heating by the exhaust gases heat exchanger, fresh air preheating heat exchanger, one end of coking furnace shaft combustion chamber is set
There are combustion head, the other end to be equipped with and mend wind heat exchanger 8,8 are equipped with heating by the exhaust gases heat exchanger, heating by the exhaust gases heat exchanger on benefit wind heat exchanger
One side connects combuster by flue, opposite side is connected to baking oven by exhaust fan, mends and is preheated on wind heat exchanger by mending wind
Machine is connected with fresh air air inlet, and combustion head is equipped with raw coal inlet, combustion fan, and combustion fan provides more oxygen and protects
Card natural gas fully burns, and several exhaust fans, filtering of the invention barrier dress are connected between baking oven 16 and benefit wind-heat exchanger 8
Put the non-woven fabrics filtration core for being provided with and absorbing large dust particle.
Coking wastewater 21 after spray head settles is by reconciling pond 22, oil removing 23, dephenolize 24, ammonia still process 25, biochemical treatment
28, the discharge of wastewater 30 after finally obtaining the waste water after deep purifying 29 or will be up to standard, and can be through overfocus in oil removing link
Oil can also pass through tar to tar ammonia water separator 26 and by ammonia steam to sulphur ammonia to tar ammonia water separator, in ammonia still process link
Or ammonolysis craft 27.The device structure is simple, repacking is convenient, cheap, waste gas circulation is fully burnt, and environment protection standard effect is good,
Save the energy, easy to spread.
It although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, can be with
Understanding without departing from the principles and spirit of the present invention can carry out these embodiments a variety of variations, modification, replace
And modification, the scope of the present invention is defined by the appended.
Claims (9)
1. a kind of energy conservation and environmental protection coking equipment, the coking equipment includes coke oven exhaust gas chimney, coking furnace shaft, and feature exists
In:It further includes high-temp waste gas recover, aspirating air pipe, exhaust fan, air collector, baking oven, exhaust gas distribution flow path, fresh air
Pipeline, the high-temp waste gas recover for absorbing exhaust gas are arranged on coke oven exhaust gas chimney, and aspirating air pipe one end connection high-temp waste gas returns
Device is received, exhaust fan is arranged on aspirating air pipe, and suction, the other end of aspirating air pipe are provided for high-temp waste gas is made to enter aspirating air pipe
Air collector one end is connected, exhaust fan is by high-temp waste gas by aspirating air pipe sucking air collector, the other end connection of air collector is dried
The air inlet of case, the exhaust outlet of baking oven are connected to the benefit wind heat exchanger entrance of coking furnace shaft, fresh air through exhaust gas distribution flow path
The benefit for entering coking furnace shaft into wind-power is provided by the fresh air air inlet of fresh air pipe by fresh air exhaust fan
Wind heat exchanger entrance connects between high-temp waste gas recover and chimney for non-tight.
2. energy conservation and environmental protection coking equipment according to claim 1, it is characterised in that:Arranged for interval is equipped in the air collector
Filtering baffling device, be provided with hole or seam on the filtering baffling device.
3. energy conservation and environmental protection coking equipment according to claim 1 or 2, it is characterised in that:Settler is further included, the precipitation
Device is arranged between filtering baffling device, which includes spray head, and the bottom of air collector is provided with precipitation
Object recovery pond.
4. energy conservation and environmental protection coking equipment according to claim 1, it is characterised in that:Exhaust gas distribution flow path and combustion chamber it
Between be provided with regulating valve.
5. energy conservation and environmental protection coking equipment according to claim 3, it is characterised in that:Further include heating by the exhaust gases heat exchanger, new
Fresh air preheat heat exchanger, one end of coking furnace shaft combustion chamber are equipped with combustion head, the other end equipped with wind heat exchanger is mended, mend wind heat exchange
Device is equipped with heating by the exhaust gases heat exchanger, and heating by the exhaust gases heat exchanger one side connects combuster by flue, opposite side passes through exhausting
Machine is connected to baking oven, mends and is connected with fresh air air inlet by mending wind preheating machine on wind heat exchanger.
6. according to claim 1-5 any one of them energy conservation and environmental protection coking equipments, it is characterised in that:The combustion head is equipped with
Raw coal inlet, combustion fan, combustion fan provide more oxygen and ensure that natural gas fully burns.
7. energy conservation and environmental protection coking equipment according to claim 5, it is characterised in that:The baking oven with mend wind-heat exchanger it
Between be connected with several exhaust fans.
8. energy conservation and environmental protection coking equipment according to claim 3, it is characterised in that:It is provided on the filtering baffling device
Absorb the non-woven fabrics filtration core of large dust particle.
9. energy conservation and environmental protection coking equipment according to claim 3, it is characterised in that:Coking wastewater after spray head settles
By reconciling pond, oil removing, dephenolize, ammonia still process biochemical treatment, the waste water after finally obtaining the waste water after deep purifying or will be up to standard
Discharge, and can pass through tar to tar ammonia water separator in oil removing link, it can will obtain sodium phenolate or phenol essence in dephenolize link
It causes, can also pass through tar to tar ammonia water separator steaming phenol link.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711472579.1A CN108059963A (en) | 2017-12-29 | 2017-12-29 | A kind of energy conservation and environmental protection coking equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711472579.1A CN108059963A (en) | 2017-12-29 | 2017-12-29 | A kind of energy conservation and environmental protection coking equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN108059963A true CN108059963A (en) | 2018-05-22 |
Family
ID=62140667
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201711472579.1A Pending CN108059963A (en) | 2017-12-29 | 2017-12-29 | A kind of energy conservation and environmental protection coking equipment |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN108059963A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108452634A (en) * | 2018-06-14 | 2018-08-28 | 王书虎 | A kind for the treatment of process and equipment of organic exhaust gas |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2463688Y (en) * | 2001-01-22 | 2001-12-05 | 武小军 | Coke-oven exhaust circulating combustion recovery plant |
JP2015003992A (en) * | 2013-06-20 | 2015-01-08 | Jfeスチール株式会社 | Exhaust gas treatment apparatus and method |
CN105885876A (en) * | 2016-05-09 | 2016-08-24 | 大连迈泰克科技开发有限公司 | Energy-saving and environment-friendly coking process method capable of realizing low NOX emission concentration in front-end treatment |
-
2017
- 2017-12-29 CN CN201711472579.1A patent/CN108059963A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2463688Y (en) * | 2001-01-22 | 2001-12-05 | 武小军 | Coke-oven exhaust circulating combustion recovery plant |
JP2015003992A (en) * | 2013-06-20 | 2015-01-08 | Jfeスチール株式会社 | Exhaust gas treatment apparatus and method |
CN105885876A (en) * | 2016-05-09 | 2016-08-24 | 大连迈泰克科技开发有限公司 | Energy-saving and environment-friendly coking process method capable of realizing low NOX emission concentration in front-end treatment |
Non-Patent Citations (1)
Title |
---|
刘建秋等: "《煤化工安全与环保》", 31 August 2015, 中国环境出版社 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108452634A (en) * | 2018-06-14 | 2018-08-28 | 王书虎 | A kind for the treatment of process and equipment of organic exhaust gas |
CN108452634B (en) * | 2018-06-14 | 2024-04-02 | 济南众焦先科环保科技有限公司 | Organic waste gas treatment process and equipment |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102851420B (en) | Steelmaking residual heat step recycling method | |
CN104110675A (en) | Deep heat recovery device and deep heat recovery method for boiler smoke | |
CN105509492A (en) | System and method for recovering waste heat and CO2 of alumina rotary kiln flue gas | |
CN209960532U (en) | Waste heat recycling system of gas boiler | |
CN206828450U (en) | A kind of energy-saving oil-based drill cuttings thermal desorption furnace system | |
CN106322427A (en) | Deslagging waste heat utilization system and deslagging waste heat utilization method for circulating fluidized bed boiler | |
CN109775785A (en) | A kind of high-salt wastewater burns desalting system and its processing method | |
CN212198516U (en) | Energy recycling system for activated carbon production | |
CN110822923B (en) | Waste heat recovery system of petrochemical heating furnace | |
CN108059963A (en) | A kind of energy conservation and environmental protection coking equipment | |
CN106853324A (en) | A kind of flue gas deep dehydration treatment and WHRS | |
CN204084324U (en) | A kind of boiler smoke degree of depth heat reclamation device | |
CN103614509B (en) | A kind of carbon steel converter dry cloth bag dedusting process of whole process recovery waste heat and device thereof | |
CN204943883U (en) | A kind of heating boiler of hot tail gas Heat Treatment device | |
CN108826269A (en) | The utilization system of fume afterheat and deslagging waste heat based on CFB boiler | |
CN212818972U (en) | Colored smoke plume desorption system of high temperature water flushing sediment steam | |
CN212293435U (en) | Waste gas recycling device for carbonization furnace | |
CN109775786A (en) | A kind of high-salt wastewater burns desalting system and its processing method | |
CN210861049U (en) | Gas boiler flue gas waste heat and condensate water recycling system | |
CN209470203U (en) | Novel super-low discharge cycle fluidized bed water-coal-slurry hot-water boiler | |
CN106918029A (en) | A kind of coking energy coupling optimization and pollutant collaboration governing system and its method | |
CN208349328U (en) | A kind of dedusting of coal-fired hot-water boiler flue gas disappears white waste heat depth recovery system | |
CN201973727U (en) | Regenerative furnace | |
CN110894954A (en) | High-temperature tail gas purification and waste heat recovery system | |
CN206478721U (en) | A kind of Circulating Cooling Water of Power Plant condensation waste heat utilizes system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180522 |