SU321535A1 - METHOD OF BASKED LOADING OF COKE OVENS 1 OF HOT OR DRY COAL MIXTURE - Google Patents
METHOD OF BASKED LOADING OF COKE OVENS 1 OF HOT OR DRY COAL MIXTUREInfo
- Publication number
- SU321535A1 SU321535A1 SU1278350A SU1278350A SU321535A1 SU 321535 A1 SU321535 A1 SU 321535A1 SU 1278350 A SU1278350 A SU 1278350A SU 1278350 A SU1278350 A SU 1278350A SU 321535 A1 SU321535 A1 SU 321535A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- loading
- hot
- coke ovens
- dry coal
- basked
- Prior art date
Links
- 239000000571 coke Substances 0.000 title claims description 6
- 238000000034 method Methods 0.000 title claims description 6
- 239000003245 coal Substances 0.000 title claims 2
- 239000000203 mixture Substances 0.000 title description 2
- 239000007789 gas Substances 0.000 claims description 13
- 238000010793 Steam injection (oil industry) Methods 0.000 claims 1
- 230000008014 freezing Effects 0.000 claims 1
- 238000007710 freezing Methods 0.000 claims 1
- 238000004939 coking Methods 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 1
Description
Предложенный способ относитс к коксохимическому производству и МО/кет быть использован при коксовании термически подготовленных шихт.The proposed method relates to coke production and MO / KET to be used in the coking of thermally prepared mixtures.
Известный способ бездымной загрузки коксовых печей путем одновременной засыпки шихты и отсоса газов загрузки через загрузочные люки предусматривает выброс газов загрузки после очистки от ныли в атмосферу, что сильно затрудн ет воздушный бассейн. The known method of smokeless loading of coke ovens by simultaneous charging of the charge and suction of the gases of the charge through the loading hatches provides for the discharge of the gases of the charge after being cleared from the atmosphere, which greatly complicates the air pool.
С целью устранени этого недостатка предлагаетс загрузку коксовых печей гор чей или сухой шихтой производить только через сред}1ий загрузочный люк, а газы загрузки отводить через крайние загрузочные люки и после очистки от пыли через систему трубопроводов сбрасывать в газосборник.In order to eliminate this drawback, it is proposed to load the coke ovens with a hot or dry charge only through media} the first loading hatch, and discharge gases from the extreme loading hatches and after cleaning from dust through the piping system to be discharged into the gas collector.
Способ состоит в следующем.The method consists in the following.
Загрузку камеры коксовой нечи гор чей или сухой шихтой производ т только через средНИИ загрузочный люк из среднего бункера загрузочного вагона, объем которого увеличен до объема коксовой камеры. Обычньп проход газов из камеры коксовани через нижний коней , сто ков в газосборник на период загрузки перекрывают, а газы загрузки отвод т через крайние загрузочные люки. Дл обеспечени взрывобезопасности газы загрузки сразу после выхода из печи проход т через футерованные трубы, снабженные электрообогревом, обеспечиваюшим на их внутренне оверхности температуру 800-1000°С, где збь точнь й кислород выгорает до безопасной коние трании . После очистки в сухих циклонах газ загрузки через систему трубопроводов в газосборник.The coking nets chamber is loaded with a hot or dry charge only through the middle institute of the loading hatch from the medium hopper of the loading car, the volume of which is increased to the volume of the coke oven chamber. The usual passage of gases from the coking chamber through the lower horses, the outflow to the gas collector during the loading period is blocked, and the loading gases are diverted through the outer loading hatches. To ensure explosion safety, the charging gases immediately after exiting the furnace pass through lined pipes equipped with electric heating, which provide a temperature of 800-1000 ° C on their internal surfaces, where the exact oxygen burns to a safe condition. After cleaning in dry cyclones gas loading through the piping system to the gas collector.
Предмет изобретени Subject invention
Claims (2)
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU321535A1 true SU321535A1 (en) |
Family
ID=
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4265709A (en) * | 1978-02-06 | 1981-05-05 | Firma Carl Still | Method and apparatus for separating gases and solids during the carbonization of coal |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4265709A (en) * | 1978-02-06 | 1981-05-05 | Firma Carl Still | Method and apparatus for separating gases and solids during the carbonization of coal |
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