CN110527529B - Coke oven regenerator adopting packing mode for heat exchange - Google Patents
Coke oven regenerator adopting packing mode for heat exchange Download PDFInfo
- Publication number
- CN110527529B CN110527529B CN201910924167.XA CN201910924167A CN110527529B CN 110527529 B CN110527529 B CN 110527529B CN 201910924167 A CN201910924167 A CN 201910924167A CN 110527529 B CN110527529 B CN 110527529B
- Authority
- CN
- China
- Prior art keywords
- regenerator
- coke oven
- filler
- heat storage
- air flow
- 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
- 239000000571 coke Substances 0.000 title claims abstract description 33
- 238000012856 packing Methods 0.000 title description 3
- 239000000945 filler Substances 0.000 claims abstract description 35
- 238000005338 heat storage Methods 0.000 claims abstract description 27
- 239000010410 layer Substances 0.000 claims abstract description 15
- 238000009825 accumulation Methods 0.000 claims abstract description 8
- 239000011229 interlayer Substances 0.000 claims abstract description 8
- 239000011449 brick Substances 0.000 claims description 6
- 210000004027 cell Anatomy 0.000 claims description 5
- 239000000919 ceramic Substances 0.000 claims description 3
- 239000002184 metal Substances 0.000 claims description 3
- 210000002421 cell wall Anatomy 0.000 claims description 2
- 210000003850 cellular structure Anatomy 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 abstract description 9
- 239000002912 waste gas Substances 0.000 abstract description 8
- 230000001174 ascending effect Effects 0.000 abstract description 3
- 238000010276 construction Methods 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 3
- 238000003763 carbonization Methods 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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
- C10B29/00—Other details of coke ovens
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Coke Industry (AREA)
- Air Supply (AREA)
Abstract
The invention relates to a coke oven regenerator adopting a filler mode for heat exchange, which comprises a random heat storage filler and an air flow distributor; and a layer of multi-layer airflow distributor is arranged in the coke oven heat storage chamber along the high direction, and random heat storage filler is filled in the upper space of the airflow distributor or in the interlayer space between the airflow distributors. The invention adopts random heat accumulation filler as a heat accumulator in the coke oven heat accumulation chamber, has simple structure and convenient construction, can quickly and efficiently absorb the heat of descending waste gas, and has higher efficiency of heating ascending lean gas or air.
Description
Technical Field
The invention relates to the technical field of coke ovens, in particular to a coke oven regenerator adopting a filler mode for heat exchange.
Background
The coke oven consists of five parts, namely a regenerator, a chute, a carbonization chamber, a combustion chamber and a furnace top; the regenerator is arranged at the lower part of the furnace body, the carbonization chambers and the combustion chambers are alternately arranged, the carbonization chambers and the combustion chambers are separated by refractory brick walls, each combustion chamber is provided with 28-36 vertical flame paths, and the inclined paths are furnace tops of the furnace body above the combustion chambers and connected with the channel carbonization chambers between the vertical flame paths of the combustion chambers and the regenerator. The gas and air for heating are preheated by high-temperature waste gas in the heat storage chamber, the preheated gas (the high-heat value gas is not preheated) and the air meet and burn at the bottom of the vertical fire channel, heat is provided for the carbonization chamber from the side face, and the coal in the carbonization chamber is heated to be changed into coke under the condition of air isolation.
When the regenerator descends high-temperature waste gas, most heat is absorbed and accumulated, so that the temperature of the waste gas is lowered from about 1200 ℃ to below 400 ℃; when the lean gas or air rises, the stored heat is transferred out, so that the lean gas or air is preheated to more than 1000 ℃. Half of the regenerators of each coke oven are always in descending air flow, and half of the regenerators are in ascending air flow, and reversing is carried out once every 20-30 minutes. At present, the conventional heat storage chambers are internally provided with checker bricks as heat storages, the dry-discharge masonry process is time-consuming and labor-consuming, the holes of the checker bricks are easy to block, the heat exchange effect is affected, and high-temperature waste gas cannot be discharged when serious, so that high-temperature accidents can be caused.
Disclosure of Invention
The invention provides a coke oven regenerator adopting a filler mode for heat exchange, which adopts random heat storage filler as a regenerator, has simple structure and convenient construction, can quickly and efficiently absorb the heat of descending waste gas, and has higher efficiency of heating ascending lean gas or air.
In order to achieve the above purpose, the invention is realized by adopting the following technical scheme:
A coke oven regenerator adopting a filler mode for heat exchange comprises random heat accumulation filler and an air flow distributor; and a layer of multi-layer airflow distributor is arranged in the coke oven heat storage chamber along the high direction, and random heat storage filler is filled in the upper space of the airflow distributor or in the interlayer space between the airflow distributors.
The coke oven regenerator is of a grid structure, and is divided into a plurality of regenerator grids from the machine side to the coke side, and each regenerator grid corresponds to one vertical flame path respectively; and a plurality of layers of air flow distributors are arranged in the inner side of each regenerator cell along the height direction, and random heat accumulation filler is filled in the upper space of each air flow distributor or in the interlayer space between each layer of air flow distributor.
The random heat storage filler is one or a mixture of a plurality of honeycomb, annular or wing random heat storage fillers.
The random heat storage filler is made of ceramic or metal.
Compared with the prior art, the invention has the beneficial effects that:
1) The random heat storage filler has good heat exchange effect, firm structure, wear resistance, easy mass production and repeated recycling;
2) The construction is convenient, compared with the existing checker brick heat accumulator, the dry-row masonry is not needed, and the time and the labor are saved;
3) One or more layers of air flow distributors are arranged, so that the air flow is more uniform, and the heat exchange effect is improved;
4) The regenerator with the cellular structure not only has better heat exchange effect, but also is beneficial to thermal regulation.
Drawings
FIG. 1 is a schematic diagram of a regenerator for a coke oven with heat exchange by packing according to the present invention.
Fig. 2 is A-A view of fig. 1.
In the figure: 1. coke oven regenerator 2, random heat storage filler 3, air flow distributor 4, regenerator dividing wall 5, small flue 6, regenerator main wall 7, regenerator single wall
Detailed Description
The following is a further description of embodiments of the invention, taken in conjunction with the accompanying drawings:
As shown in fig. 1 and 2, the coke oven regenerator adopting the filler mode for heat exchange comprises a random heat storage filler 2 and an airflow distributor 3; a layer of multi-layer air flow distributor 3 is arranged in the inner edge of the coke oven regenerator 1 along the height direction, and random heat accumulation filler 2 is filled in the upper space of the air flow distributor 3 or in the interlayer space between the air flow distributors 3 of each layer.
The coke oven regenerator 1 is of a grid structure, and is divided into a plurality of regenerators from the machine side to the coke side, and each regenerator corresponds to one vertical flame path respectively; and a plurality of layers of air flow distributors 3 are arranged in each regenerator cell along the height direction, and random heat accumulation filler 2 is filled in the upper space of each air flow distributor 3 or in the interlayer space between each layer of air flow distributor 3.
The random heat storage filler 2 is one or a mixture of a plurality of honeycomb, annular or wing random heat storage fillers.
The random heat storage filler 2 is made of ceramic or metal.
As shown in the figures and fig. 2, the coke oven regenerator 1 is a space at the lower part of the coke oven body separated by a main wall of the regenerator and a single wall of the regenerator, a small flue 5 is arranged below the coke oven regenerator 1, and the top of the small flue is provided with grate bricks which are separated from the regenerator; the regenerator cell walls 4 are built between the regenerator main walls 6 and the regenerator single walls 7. The multi-layer airflow distributors 3 are arranged along the high direction of the coke oven regenerator 1, and random heat storage filler 2 is filled in the interlayer space between the airflow distributors 3, and the random heat storage filler 2 fills the whole interlayer space.
When the coke oven regenerator 1 descends high-temperature waste gas, the random heat storage filler 2 absorbs and accumulates most of heat, and when lean gas or air ascends, the random heat storage filler 2 transfers the accumulated heat to heat the lean gas or air, so that the high-efficiency recovery of the waste gas heat is realized.
The random heat storage filler 2 can be formed by mixing honeycomb, annular, wing-shaped random heat storage fillers with different shapes, and the like, so that the heat exchange area is increased.
The foregoing is only a preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art, who is within the scope of the present invention, should make equivalent substitutions or modifications according to the technical scheme of the present invention and the inventive concept thereof, and should be covered by the scope of the present invention.
Claims (2)
1. A coke oven regenerator adopting a filler mode for heat exchange is characterized by comprising random heat accumulation filler and an air flow distributor; the coke oven regenerator is a space at the lower part of the coke oven body, which is partitioned by a main wall of the regenerator and a single wall of the regenerator, a small flue is arranged below the coke oven regenerator, and the top of the small flue is provided with grate bricks which are partitioned from the regenerator; the coke oven regenerator is of a cellular structure, and is divided into a plurality of regenerator cells from the machine side to the coke side, and regenerator cell walls are built between a regenerator main wall and a regenerator single wall; each regenerator cell corresponds to one vertical flame path respectively; a plurality of layers of air flow distributors are arranged in each regenerator cell along the height direction, and random heat accumulation filler is filled in the upper space of each air flow distributor or in the interlayer space between each layer of air flow distributor; the random heat storage filler is formed by mixing honeycomb, annular and wing-shaped random heat storage fillers.
2. The coke oven regenerator of claim 1 in which the random heat storage filler is ceramic or metal.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910924167.XA CN110527529B (en) | 2019-09-27 | 2019-09-27 | Coke oven regenerator adopting packing mode for heat exchange |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910924167.XA CN110527529B (en) | 2019-09-27 | 2019-09-27 | Coke oven regenerator adopting packing mode for heat exchange |
Publications (2)
Publication Number | Publication Date |
---|---|
CN110527529A CN110527529A (en) | 2019-12-03 |
CN110527529B true CN110527529B (en) | 2024-06-07 |
Family
ID=68670603
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201910924167.XA Active CN110527529B (en) | 2019-09-27 | 2019-09-27 | Coke oven regenerator adopting packing mode for heat exchange |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN110527529B (en) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0728945U (en) * | 1993-10-26 | 1995-05-30 | 住友金属工業株式会社 | Coke oven heat storage room |
RU2088852C1 (en) * | 1992-08-28 | 1997-08-27 | Вадим Михайлович Колеватов | Straight-flow reversible heat-accumulating heating column |
CN206617946U (en) * | 2017-02-20 | 2017-11-07 | 常州创美环境科技有限公司 | Integral type RTO regenerative oxidation stoves |
CN210855974U (en) * | 2019-09-27 | 2020-06-26 | 中冶焦耐(大连)工程技术有限公司 | Coke oven regenerator adopting packing mode for heat exchange |
-
2019
- 2019-09-27 CN CN201910924167.XA patent/CN110527529B/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2088852C1 (en) * | 1992-08-28 | 1997-08-27 | Вадим Михайлович Колеватов | Straight-flow reversible heat-accumulating heating column |
JPH0728945U (en) * | 1993-10-26 | 1995-05-30 | 住友金属工業株式会社 | Coke oven heat storage room |
CN206617946U (en) * | 2017-02-20 | 2017-11-07 | 常州创美环境科技有限公司 | Integral type RTO regenerative oxidation stoves |
CN210855974U (en) * | 2019-09-27 | 2020-06-26 | 中冶焦耐(大连)工程技术有限公司 | Coke oven regenerator adopting packing mode for heat exchange |
Non-Patent Citations (1)
Title |
---|
蜂窝陶瓷蓄热体的研究现状;周娴等;《陶瓷》;20090430;53-56 * |
Also Published As
Publication number | Publication date |
---|---|
CN110527529A (en) | 2019-12-03 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN201321381Y (en) | Novel carbon tank type calciner | |
CN102250629A (en) | Coking furnace capable of recycling heat energy and coking method | |
CN202465585U (en) | Tamping coke oven with combustors heated sectionally and regenerative chambers adjusted separately | |
CN202754941U (en) | Stamp-charging coke oven with partition-adjustable regenerative chambers | |
CN102627976B (en) | Coking chamber for pulverized coal destructive distillation | |
CN201314783Y (en) | Tank-type calcining furnace | |
CN102634359B (en) | Air guide brick and air guide wall thereof as well as pulverized coal destructive distillation carbonization chamber applying brick and wall | |
CN104593015A (en) | Formcoke refining method and device thereof | |
CN210855974U (en) | Coke oven regenerator adopting packing mode for heat exchange | |
CN103740383B (en) | Transverse reciprocating heating system of coke oven | |
CN110527529B (en) | Coke oven regenerator adopting packing mode for heat exchange | |
CN103834416A (en) | Large-sized tamping coke oven | |
CN201262514Y (en) | Chamber type coal ash haydite sintering furnace | |
US3102846A (en) | Coking retort oven with liner walls of two thicknesses | |
CN202322715U (en) | Novel stamp-charging coke oven | |
CN107936999B (en) | Bidirectional heating system and heating method of external heating type low-order pulverized coal continuous carbonization furnace | |
CN215799310U (en) | Coke oven regenerator structure | |
CN211367621U (en) | Top combustion hot blast stove with tapered regenerative chamber | |
CN103773394A (en) | Transverse alternative heating and vertical coke exhaust coke oven | |
CN203668305U (en) | Horizontal alternative heating and vertical coke discharging type coke oven | |
CN101398259B (en) | Bottom flue gas passage structure of electrode calcination furnace with cap | |
CN107903920B (en) | Heat storage chamber of vertical furnace | |
CN103740382B (en) | Transverse alternate heating system of coke oven | |
CN202322714U (en) | Novel stamp-charging coke oven with wide coking chamber | |
CN207030963U (en) | Absorbent charcoal activation furnace |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant |