CN102304369B - Oven-drying working process for coke dry quenching system - Google Patents
Oven-drying working process for coke dry quenching system Download PDFInfo
- Publication number
- CN102304369B CN102304369B CN 201110231265 CN201110231265A CN102304369B CN 102304369 B CN102304369 B CN 102304369B CN 201110231265 CN201110231265 CN 201110231265 CN 201110231265 A CN201110231265 A CN 201110231265A CN 102304369 B CN102304369 B CN 102304369B
- Authority
- CN
- China
- Prior art keywords
- oven
- dried
- boiler
- stove
- drying
- 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.)
- Active
Links
Images
Abstract
The invention discloses an oven-drying working process for a coke dry quenching system. The process comprises the following steps: step 1, drying a dry quenching oven with warm wind; step 2, drying the dry quenching oven with coal gas after the step 1 is finished; and step 3, after the step 2 is finished, putting red-hot coke in the dry quenching oven so that a refractory material is heated to 950-1050 DEG C at the speed of less than or equal to 30 DEG C/h, thereby completing the oven-drying operation. According to the oven-drying working process for the coke dry quenching system, in the warm wind drying process, the temperature of a boiler collecting box is in conformity with the temperature of a steam pocket, thus the gap generated due to the tremble of the boiler when an airlift pump works is avoided so that boiler steam can not be intermixed with dry air, thereby correctly and timely judging the drying condition of the dry quenching oven; and in the coal gas drying stage, the refractory material is heated according to a heating crystal form conversion curve through reasonably controlling the coal gas-air proportion and heating speed, thereby avoiding the conditions that mixed coal gas extinguishes, the refractory material is broken or damaged, and the like. Thus, by the process disclosed by the invention, the service life of the dry quenching oven refractory material can be prolonged, the safe work of a boiler system can be ensured and the service life of the boiler system is prolonged, and oven-drying working time can be shortened at the same time.
Description
Technical field
The present invention relates to a kind of coking technology field, particularly a kind of roast technic of dry quenching system.
Background technology
Need body of heater is dried before coke dry quenching furnace is gone into operation, separating out the moisture of refractory materials in the stove, and body of heater is heated up, thereby be connected with the normal production red furnace temperature when burnt of packing into, prevent refractory materials cracking of building body or damage.
In the prior art, oven-drying working process for coke dry quenching system is divided into altogether three phases, and the fs is the warm air drying stage, and its main purpose is that the dried refractory materials moisture content that puts out in the stove is separated out; Subordinate phase is the coal gas baker stage, need prevent refractory materials cracking of building body or damage; Phase III, this stage mainly was when continuing to guarantee that the coke oven masonry heats up by curve, lays the first stone for guaranteeing the adjustment of producing each parameter as a trial in order to throw the red burnt stage.
Mainly there is following defective in existing technique:
1, in the warm air drying stage, because boiler header water temperature and drum temperature differ larger, cause boiler systems to tremble, easily make the damage boiler cause steam to sneak into the oven dry air, thus the dried oven dry situation of putting out stove of judgement that can't be promptly and accurately.
2, in the coal gas baking stage, because the control of the proportioning of coke-oven gas and air is relatively poor, at the coal gas baking stage flame-out, the dried oven refractory that puts out occuring easily can not heat up according to intensification transformation of crystal curve, easily causes refractory materials to break or damages.
Therefore need to improve oven-drying working process for coke dry quenching system of the prior art, to overcome defective of the prior art.
Summary of the invention
In view of this, the purpose of this invention is to provide a kind of oven-drying working process for coke dry quenching system, can prevent that at the warm air drying stage boiler systems from trembling, avoid damage in boilers the slit to occur and make steam sneak into the oven dry air, cause can't be promptly and accurately the dried oven dry situation of putting out stove of judgement; And in the coal gas baking stage, accurately control the proportioning of coke-oven gas and air, and avoid flame-out, the dried oven refractory that puts out of coal gas baking stage to heat up not according to intensification transformation of crystal curve, cause refractory materials to break or damage.The concrete scheme of this technique is:
Oven-drying working process for coke dry quenching system of the present invention may further comprise the steps:
Step 1, the dried stove that puts out of warm air oven dry,
Step 2, after step 1 finishes, carry out the dried stove that puts out of coal gas oven dry,
Step 3, after step 2 finishes, put out red Jiao that packs in the stove and make refractory materials be warming up to 950-1050 ℃ with the speed of≤30 ℃/h to dried, finish the baker operation, in this process continuously to dried put out pass in the stove nitrogen with stove in inflammable gas cement out, the refractory materials heat-up rate is less in this step, can guarantee that more refractory materials is not damaged and breaks, but baker is consuming time longer, allowing heat-up rate in the temperature-rise period is 0 state, be keeping warm mode, and the heat-up rate of different time sections can change in the whole temperature-rise period;
Described step 1 comprises following operation:
A, air is passed into boiler, boiler utilizes low-pressure steam that air is heated, and before the work of boiler airlift pump, makes the boiler header water temperature reach consistent with the drum temperature by the boiler evaporator continuous blowdown;
B, will dry it from the boiler dried stove that puts out of warm air input out, until till the dried moisture that puts out in the oven refractory all separated out, the dried stove chamber pressure that prestores that puts out is controlled at 55-65Pa in the drying course;
Described step 2 comprises following operation:
I, coal gas and air are mixed into air mixture for 1:5 by volume, air mixture is passed into the dried stove burning of putting out, make the dried oven refractory that puts out with the speed intensification of≤3.3 ℃/h, until furnace temperature rises to till 790-810 ℃, the refractory materials heat-up rate is less in this operation, can guarantee that more refractory materials is not damaged and breaks, but baker is consuming time longer, allowing heat-up rate in the temperature-rise period is 0 state, be keeping warm mode, and the heat-up rate of different time sections can change in the whole temperature-rise period.
Further, behind described operation b, also be provided with operation c: the dried stove air input cleaning apparatus out that puts out is carried out dust removal process, will enter atmosphere through the air of dust removal process;
Further, among the described operation b, the dried oven refractory speed with 10 ℃/h in by the hot air dries process of putting out heats up;
Further, after the operation I, also be provided with the operation II: will enter atmosphere from the dried waste gas part of discharging the stove of putting out after the burning in the operation I, another part is sent into boiler through the first time after the dust removal process to be heated, to carrying out the dust removal process second time from boiler this part gas out, will through the second time dust removal process gas input the dried stove that puts out with the air mixture described in the operation I.
Beneficial effect of the present invention: oven-drying working process for coke dry quenching system of the present invention, in the warm air drying course, the temperature of boiler header and drum is consistent, avoid airlift pump when work boiler to tremble and produced the gap, Boiler Steam can not sneaked into the oven dry air, thereby can accurately and timely judge the dried dried situation of bake oven of putting out; At the coal gas baking stage, by rational control coal gas air proportioning and heat-up rate, refractory materials is heated up according to intensification transformation of crystal curve, avoided that air mixture is flame-out, refractory materials breaks or the situation such as damage; Thereby this technique can prolong dried work-ing life of putting out oven refractory, guarantees the boiler systems trouble-free service and prolongs its work-ing life, can shorten the oven-drying working time simultaneously.
Description of drawings
The invention will be further described below in conjunction with drawings and Examples.
Fig. 1 is oven-drying working process for coke dry quenching system warm air baker flow chart of steps of the present invention;
Fig. 2 is oven-drying working process for coke dry quenching system coal gas baker flow chart of steps of the present invention.
Embodiment
Fig. 1 is oven-drying working process for coke dry quenching system warm air baker flow chart of steps of the present invention; Fig. 2 is oven-drying working process for coke dry quenching system coal gas baker flow chart of steps of the present invention.
Embodiment one: as shown in the figure, oven-drying working process for coke dry quenching system may further comprise the steps:
Step 1, the dried stove that puts out of warm air oven dry,
Step 2, after step 1 finishes, carry out the dried stove that puts out of coal gas oven dry,
Step 3, after step 2 finishes, put out red Jiao that packs in the stove and make refractory materials be warming up to 1050 ℃ with 30 ℃/h speed to dried, finish the baker operation, in this process continuously to dried put out pass in the stove nitrogen with stove in inflammable gas cement out, inflammable gas is cemented out can avoid inflammable gas to gather the danger of blasting; Drop into red Jiao the dried stove that puts out is heated up, can to the dried stove test data before the formula work of becoming a full member of putting out, guarantee that the dried stove life's work that puts out carries out smoothly; Certainly in implementation, the refractory materials heat-up rate can also be other value in＜30 ℃/h scope in this step, the refractory materials outlet temperature also can be other values in 950-1050 ℃ of scopes, and allowing heat-up rate in the temperature-rise period is 0 state, be keeping warm mode, and the heat-up rate of different time sections can change in the whole temperature-rise period; Dried in implementation to put out the oven refractory heat-up rate less, can guarantee that more refractory materials is not damaged and breaks, but baker is consuming time longer, is unfavorable in time entering the normal production phase.Refractory materials heats up with 30 ℃/h speed and can both guarantee that refractory materials can not damage and break in this step, can also guarantee that the dried oven refractory that puts out reaches dried temperature when putting out stove and becoming a full member normal production with the shortest time.In this operation dried put out oven refractory reach with different heat-up rates processing requirement the temperature embodiment will be in the subsequent embodiment illustrated.
Described step 1 comprises following operation:
A, air is passed into boiler, boiler utilizes low-pressure steam that air is heated, and before the work of boiler airlift pump, make the boiler header water temperature reach consistent with the drum temperature by the boiler evaporator continuous blowdown, the temperature of boiler header and drum is consistent, avoided airlift pump when work boiler to tremble and produce the gap, Boiler Steam can not sneaked into the oven dry air, thereby can accurately and timely judge the dried dried situation of bake oven of putting out;
B, will dry it from the boiler dried stove that puts out of warm air input out, until till the dried moisture that puts out in the oven refractory all separated out, the dried stove chamber pressure that prestores that puts out is controlled at 55-65Pa in the drying course, in the drying course the dried stove chamber pressure fluctuation range that prestores of putting out is controlled at 55-65Pa, can guarantee the dried oven refractory heat-up rate equilibrium of putting out, avoid damaging refractory materials;
Described step 2 comprises following operation:
I, with coal gas and air by volume for 1:5 is mixed into air mixture, air mixture is passed into the dried stove burning of putting out, the dried oven refractory that puts out is heated up, until furnace temperature rises to till 810 ℃ with the speed of 3.3 ℃/h; By rational control coal gas air proportioning and heat-up rate, refractory materials is heated up according to intensification transformation of crystal curve, avoided that air mixture is flame-out, refractory materials breaks or the situation such as damage.Certainly in implementation, the refractory materials heat-up rate can also be other value in＜3.3 ℃/h scope in this step, the refractory materials outlet temperature also can be other values in 790-810 ℃ of scopes, and allowing heat-up rate in the temperature-rise period is 0 state, be keeping warm mode, and the heat-up rate of different time sections can change in the whole temperature-rise period; Dried in implementation to put out the oven refractory heat-up rate less, can guarantee that more refractory materials is not damaged and breaks, but baker is consuming time longer, is unfavorable in time entering the normal production phase.Refractory materials heats up with 3.3 ℃/h speed and can both guarantee that refractory materials can not damage and break in this step, can also guarantee the dried oven refractory that puts out with the shortest time completing steps 2, is conducive to the dried stove that puts out and in time changes normal production over to.In this operation dried put out oven refractory reaches the temperature of processing requirement with different heat-up rates embodiment will be in the subsequent embodiment illustrated.
Adopt this technique can prolong dried work-ing life of putting out oven refractory, guarantee the boiler systems trouble-free service and prolong its work-ing life, can shorten the oven-drying working time simultaneously.
As the improvement to the present embodiment, behind described operation b, also be provided with operation c: the dried stove air input cleaning apparatus out that puts out is carried out dust removal process, to enter atmosphere through the air of dust removal process, this operation can be removed from the dried stove airborne dust out that puts out, and avoids atmosphere is polluted.
As the improvement to the present embodiment, among the described operation b, the dried oven refractory that puts out heats up with the speed of 10 ℃/h in by the hot air dries process, both can obtain faster drying efficiency, can guarantee that refractory materials does not break and damages simultaneously.
As the improvement to the present embodiment, after the operation I, also be provided with the operation II: will enter atmosphere from the dried waste gas part of discharging the stove of putting out after the burning in the operation I, another part is sent into boiler through the first time after the dust removal process to be heated, to carrying out the dust removal process second time from boiler this part gas out, will through the second time dust removal process gas input the dried stove that puts out with the air mixture described in the operation I; This operation has reclaimed that part is dried puts out the waste gas that fire grate goes out, utilize the heat energy of waste gas the more dried stove that puts out to be dried, can save a large amount of coal gas, be conducive to reduce the oven dry cost, and the waste gas to recycling has carried out dust removal process, can remove the dried dust that puts out in the stove, and can avoid dust that boiler is caused damage.
Embodiment two: as shown in the figure, oven-drying working process for coke dry quenching system may further comprise the steps:
Step 1, the dried stove that puts out of warm air oven dry,
Step 2, after step 1 finishes, carry out the dried stove that puts out of coal gas oven dry,
Step 3, after step 2 finishes, put out red Jiao that packs in the stove and make refractory materials be warming up to 1000 ℃ with 25 ℃/h speed to dried, finish the baker operation, in this process continuously to dried put out pass in the stove nitrogen with stove in inflammable gas cement out, inflammable gas is cemented out can avoid inflammable gas to gather the danger of blasting; Drop into red Jiao the dried stove that puts out is heated up, can to the dried stove test data before the formula work of becoming a full member of putting out, guarantee that the dried stove life's work that puts out carries out smoothly;
Described step 1 comprises following operation:
A, air is passed into boiler, boiler utilizes low-pressure steam that air is heated, and before the work of boiler airlift pump, make the boiler header water temperature reach consistent with the drum temperature by the boiler evaporator continuous blowdown, the temperature of boiler header and drum is consistent, avoided airlift pump when work boiler to tremble and produce the gap, Boiler Steam can not sneaked into the oven dry air, thereby can accurately and timely judge the dried dried situation of bake oven of putting out;
B, will dry it from the boiler dried stove that puts out of warm air input out, until till the dried moisture that puts out in the oven refractory all separated out, the dried stove chamber pressure that prestores that puts out is controlled at 55-65Pa in the drying course, in the drying course the dried stove chamber pressure fluctuation range that prestores of putting out is controlled at 55-65Pa, can guarantee the dried oven refractory heat-up rate equilibrium of putting out, avoid damaging refractory materials;
Described step 2 comprises following operation:
I, with coal gas and air by volume for 1:5 is mixed into air mixture, air mixture is passed into the dried stove burning of putting out, the dried oven refractory that puts out is heated up, until furnace temperature rises to till 800 ℃ with the speed of 2.5 ℃/h; By rational control coal gas air proportioning and heat-up rate, refractory materials is heated up according to intensification transformation of crystal curve, avoided that air mixture is flame-out, refractory materials breaks or the situation such as damage.
Adopt this technique can prolong dried work-ing life of putting out oven refractory, guarantee the boiler systems trouble-free service and prolong its work-ing life, can shorten the oven-drying working time simultaneously.
As the improvement to the present embodiment, behind described operation b, also be provided with operation c: the dried stove air input cleaning apparatus out that puts out is carried out dust removal process, to enter atmosphere through the air of dust removal process, this operation can be removed from the dried stove airborne dust out that puts out, and avoids atmosphere is polluted.
As the improvement to the present embodiment, among the described operation b, the dried oven refractory that puts out heats up with the speed of 10 ℃/h in by the hot air dries process, both can obtain faster drying efficiency, can guarantee that refractory materials does not break and damages simultaneously.
As the improvement to the present embodiment, after the operation I, also be provided with the operation II: will enter atmosphere from the dried waste gas part of discharging the stove of putting out after the burning in the operation I, another part is sent into boiler through the first time after the dust removal process to be heated, to carrying out the dust removal process second time from boiler this part gas out, will through the second time dust removal process gas input the dried stove that puts out with the air mixture described in the operation I; This operation has reclaimed that part is dried puts out the waste gas that fire grate goes out, utilize the heat energy of waste gas the more dried stove that puts out to be dried, can save a large amount of coal gas, be conducive to reduce the oven dry cost, and the waste gas to recycling has carried out dust removal process, can remove the dried dust that puts out in the stove, and can avoid dust that boiler is caused damage.
Embodiment three: as shown in the figure, oven-drying working process for coke dry quenching system may further comprise the steps:
Step 1, the dried stove that puts out of warm air oven dry,
Step 2, after step 1 finishes, carry out the dried stove that puts out of coal gas oven dry,
Step 3, after step 2 finishes, put out red Jiao that packs in the stove and make refractory materials be warming up to 950 ℃ with 20 ℃/h speed to dried, finish the baker operation, in this process continuously to dried put out pass in the stove nitrogen with stove in inflammable gas cement out, inflammable gas is cemented out can avoid inflammable gas to gather the danger of blasting; Drop into red Jiao the dried stove that puts out is heated up, can to the dried stove test data before the formula work of becoming a full member of putting out, guarantee that the dried stove life's work that puts out carries out smoothly;
Described step 1 comprises following operation:
A, air is passed into boiler, boiler utilizes low-pressure steam that air is heated, and before the work of boiler airlift pump, make the boiler header water temperature reach consistent with the drum temperature by the boiler evaporator continuous blowdown, the temperature of boiler header and drum is consistent, avoided airlift pump when work boiler to tremble and produce the gap, Boiler Steam can not sneaked into the oven dry air, thereby can accurately and timely judge the dried dried situation of bake oven of putting out;
B, will dry it from the boiler dried stove that puts out of warm air input out, until till the dried moisture that puts out in the oven refractory all separated out, the dried stove chamber pressure that prestores that puts out is controlled at 65Pa in the drying course, in the drying course the dried stove chamber pressure fluctuation range that prestores of putting out is controlled at 55-65Pa, can guarantee the dried oven refractory heat-up rate equilibrium of putting out, avoid damaging refractory materials;
Described step 2 comprises following operation:
I, with coal gas and air by volume for 1:5 is mixed into air mixture, air mixture is passed into the dried stove burning of putting out, the dried oven refractory that puts out is heated up, until furnace temperature rises to till 790 ℃ with the speed of 2 ℃/h; By rational control coal gas air proportioning and heat-up rate, refractory materials is heated up according to intensification transformation of crystal curve, avoided that air mixture is flame-out, refractory materials breaks or the situation such as damage.
Adopt this technique can prolong dried work-ing life of putting out oven refractory, guarantee the boiler systems trouble-free service and prolong its work-ing life, can shorten the oven-drying working time simultaneously.
As the improvement to the present embodiment, behind described operation b, also be provided with operation c: the dried stove air input cleaning apparatus out that puts out is carried out dust removal process, to enter atmosphere through the air of dust removal process, this operation can be removed from the dried stove airborne dust out that puts out, and avoids atmosphere is polluted.
As the improvement to the present embodiment, among the described operation b, the dried oven refractory that puts out heats up with the speed of 10 ℃/h in by the hot air dries process, both can obtain faster drying efficiency, can guarantee that refractory materials does not break and damages simultaneously.
As the improvement to the present embodiment, after the operation I, also be provided with the operation II: will enter atmosphere from the dried waste gas part of discharging the stove of putting out after the burning in the operation I, another part is sent into boiler through the first time after the dust removal process to be heated, to carrying out the dust removal process second time from boiler this part gas out, will through the second time dust removal process gas input the dried stove that puts out with the air mixture described in the operation I; This operation has reclaimed that part is dried puts out the waste gas that fire grate goes out, utilize the heat energy of waste gas the more dried stove that puts out to be dried, can save a large amount of coal gas, be conducive to reduce the oven dry cost, and the waste gas to recycling has carried out dust removal process, can remove the dried dust that puts out in the stove, and can avoid dust that boiler is caused damage.
Embodiment four: the difference of the present embodiment oven-drying working process for coke dry quenching system and embodiment 1 only is: 1, in the operation I of described step 2, the dried oven refractory that puts out is to heat up with the speed of 1.5 ℃/h, until furnace temperature rises to 800 ℃; 2, in step 3, the dried oven refractory that puts out is to be warming up to 1000 ℃ with 15 ℃/h speed.
Embodiment five: the difference of the present embodiment oven-drying working process for coke dry quenching system and embodiment 1 only is: 1, in the operation I of described step 2, the dried oven refractory that puts out is to heat up with the speed of 1 ℃/h, until furnace temperature rises to 805 ℃; 2, in step 3, the dried oven refractory that puts out is to be warming up to 1020 ℃ with 10 ℃/h speed.
Embodiment six: the difference of the present embodiment oven-drying working process for coke dry quenching system and embodiment 1 only is: 1, in the operation I of described step 2, the dried oven refractory that puts out is to heat up with the speed of 0.5 ℃/h, until furnace temperature rises to 800 ℃; 2, in step 3, the dried oven refractory that puts out is to be warming up to 970 ℃ with 5 ℃/h speed.
Embodiment seven: the difference of the present embodiment oven-drying working process for coke dry quenching system and embodiment 1 only is: 1, in the operation I of described step 2, the dried oven refractory that puts out is to heat up with the speed of 0.3 ℃/h, until furnace temperature rises to 795 ℃; 2, in step 3, the dried oven refractory that puts out is to be warming up to 1050 ℃ with 3 ℃/h speed.
Explanation is at last, above embodiment is only unrestricted in order to technical scheme of the present invention to be described, although with reference to preferred embodiment the present invention is had been described in detail, those of ordinary skill in the art is to be understood that, can make amendment or be equal to replacement technical scheme of the present invention, and not breaking away from aim and the scope of technical solution of the present invention, it all should be encompassed in the middle of the claim scope of the present invention.
Claims (4)
1. oven-drying working process for coke dry quenching system is characterized in that: may further comprise the steps:
Step 1, the dried stove that puts out of warm air oven dry,
Step 2, after step 1 finishes, carry out the dried stove that puts out of coal gas oven dry,
Step 3, after step 2 finishes, put out red Jiao that packs in the stove and make refractory materials be warming up to 950-1050 ℃ with the speed of≤30 ℃/h to dried, finish the baker operation, in this process continuously to dried put out pass in the stove nitrogen with stove in inflammable gas cement out;
Described step 1 comprises following operation:
A, air is passed into boiler, boiler utilizes low-pressure steam that air is heated, and before the work of boiler airlift pump, makes the boiler header water temperature reach consistent with the drum temperature by the boiler evaporator continuous blowdown;
B, will dry it from the boiler dried stove that puts out of warm air input out, until till the dried moisture that puts out in the oven refractory all separated out, the dried stove chamber pressure that prestores that puts out is controlled at 55-65Pa in the drying course;
Described step 2 comprises following operation:
I, with coal gas and air by volume for 1:5 is mixed into air mixture, air mixture is passed into the dried stove burning of putting out, the dried oven refractory that puts out is heated up, until furnace temperature rises to till 790-810 ℃ with the speed of≤3.3 ℃/h.
2. oven-drying working process for coke dry quenching system according to claim 1 is characterized in that: also be provided with operation c behind described operation b: the dried stove air input cleaning apparatus out that puts out is carried out dust removal process, will enter atmosphere through the air of dust removal process.
3. oven-drying working process for coke dry quenching system according to claim 2 is characterized in that: among the described operation b, the dried oven refractory speed with 10 ℃/h in by the hot air dries process of putting out heats up.
4. oven-drying working process for coke dry quenching system according to claim 1, it is characterized in that: after the operation I, also be provided with the operation II: will enter atmosphere from the dried waste gas part of discharging the stove of putting out after the burning in the operation I, another part is sent into boiler through the first time after the dust removal process to be heated, to carrying out the dust removal process second time from boiler this part gas out, will through the second time dust removal process gas input the dried stove that puts out with the air mixture described in the operation I.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110231265 CN102304369B (en) | 2011-08-12 | 2011-08-12 | Oven-drying working process for coke dry quenching system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110231265 CN102304369B (en) | 2011-08-12 | 2011-08-12 | Oven-drying working process for coke dry quenching system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102304369A CN102304369A (en) | 2012-01-04 |
| CN102304369B true CN102304369B (en) | 2013-03-27 |
Family
ID=45378289
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201110231265 Active CN102304369B (en) | 2011-08-12 | 2011-08-12 | Oven-drying working process for coke dry quenching system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102304369B (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108397977B (en) * | 2017-02-05 | 2020-03-31 | 鞍钢股份有限公司 | Method for drying coke dry quenching furnace by warm air |
| CN106929038B (en) * | 2017-02-16 | 2019-11-08 | 宣化钢铁集团有限责任公司 | A kind of pair of dry coke quenching auxiliary uses the red burnt method for carrying out baker |
| CN106967448B (en) * | 2017-04-07 | 2020-06-12 | 安阳钢铁股份有限公司 | Oven drying method for dry quenching system after large-area replacement of refractory |
| CN114736697A (en) * | 2022-04-13 | 2022-07-12 | 山东四化环保节能工程有限公司 | Heating method of dry quenching furnace |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101747913A (en) * | 2009-12-31 | 2010-06-23 | 山西太钢不锈钢股份有限公司 | Method for baking dry quenching furnace |
-
2011
- 2011-08-12 CN CN 201110231265 patent/CN102304369B/en active Active
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101747913A (en) * | 2009-12-31 | 2010-06-23 | 山西太钢不锈钢股份有限公司 | Method for baking dry quenching furnace |
Non-Patent Citations (2)
| Title |
|---|
| 干熄焦系统烘炉开工制度的确定;钱虎林等;《燃料与化工》;20050331;第36卷(第2期);第15～17页第1～3部分、图1 * |
| 钱虎林等.干熄焦系统烘炉开工制度的确定.《燃料与化工》.2005,第36卷(第2期),第15～17页第1～3部分、图1. |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102304369A (en) | 2012-01-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107075379B (en) | Coke ovens with improved exhaust gas delivery in the secondary heating chamber | |
| CN102304369B (en) | Oven-drying working process for coke dry quenching system | |
| CN102295282B (en) | Carbonization-activation integral furnace | |
| KR20120120162A (en) | Method for compensating flue gas enthalpy losses of heat-recovery coke ovens | |
| CN103145328B (en) | A kind of method of basalt blast furnace slag in preparation of rock wool board comprehensive utilization | |
| CN103123224B (en) | Open-type roasting furnace heating curve and furnace moving operational method | |
| CN101353579B (en) | 7.63m coke oven negative pressure in-furnace furnace drying method | |
| CN104019446A (en) | Energy-saving environmentally-friendly boiler baking method for CFB boiler wear-resisting lining engineering | |
| CN102564109B (en) | Irregular furnace moving operation and warming method for turning furnace chambers of roasting furnace | |
| CN103014310B (en) | Timing constant-temperature reversing device of regenerative furnace and method thereof | |
| CN102344133A (en) | Method for preparing fine particles high-density graphite product and open type circular calcinator | |
| CN104817084B (en) | calcium carbide smelting furnace | |
| CN101121893A (en) | Method for controlling flue suction force in coke oven automatic heating system | |
| CN103740380B (en) | A kind of heatingup of coke oven battery technique | |
| CN108278854A (en) | A kind of diesel oil furnace drying method | |
| CN108865185A (en) | A kind of charing chamber pressure is positive the heatingup of coke oven battery technique of pressure | |
| CN108793781A (en) | A kind of energy-saving and environment-friendly twin furnace lime burner furnace | |
| CN103588401B (en) | Coal gas of converter dries calcining furnace and the furnace drying method of desulfurated plaster | |
| CN103961955A (en) | Preheating process of dust remover for filtering combustible dusty gas | |
| CN205156318U (en) | High -efficient heating furnace of chemical industry | |
| CN102767957A (en) | Boiler drying temperature control module and its control method | |
| CN104498071B (en) | The heating means of accumulation of heat intermittent-heating stove in oil shale retorting oil refining | |
| CN103591812A (en) | Method of clearing coke in tube heating furnace | |
| CN103664008A (en) | Low-temperature control process for oven baking of annular sleeve kiln | |
| CN103743243A (en) | Method for raising temperature of nickel flash furnace |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190211 Address after: 401220 No. 1, Gangcheng Road, Changshou District, Chongqing Patentee after: Chongqing Iron and Steel Co., Ltd. Address before: 400081 No. three, Tai Yan village, Dadukou District, Chongqing Patentee before: Chongqing Iron & Steel (Group) Co., Ltd. |
|
| CP02 | Change in the address of a patent holder | ||
| CP02 | Change in the address of a patent holder |
Address after: No.2 Jiangnan Avenue, Jiangnan street, Changshou District, Chongqing 401220 Patentee after: CHONGQING IRON & STEEL Co.,Ltd. Address before: 401220 No. 1, Gangcheng Road, Changshou District, Chongqing Patentee before: CHONGQING IRON & STEEL Co.,Ltd. |