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    • 4. 发明专利
    • METHOD AND APPARATUS FOR MEASUREMENT OF WORN-OUT AMOUNT OF OVEN WALL OF COKE OVEN
    • JPH07243812A
    • 1995-09-19
    • JP3350294
    • 1994-03-03
    • KAWASAKI STEEL CO
    • OSADA YASUSHIAIHARA TSUNEOSUGIBE HIDETAKA
    • G01B11/00C10B41/00F27D1/00G01C3/06
    • PURPOSE:To measure the worn-out amount of the right oven wall and the left oven wall of a carbonization chamber with high accuracy by a method wherein a criterion value which has been corrected according to the advance direction of a ram head is subtracted from a measured value. CONSTITUTION:A plurality of sensors 1 are installed at equal intervals in the height direction at a ram head 2 for an extruder. The extruder is pushed into from the entrance part of a carbonization chamber, a distance up to an oven wall 6 is the measured by a correction sensor 8 at the junction part of the head 2 to a rod 3 and an initial measured value t1 is used as a criterion value in the width direction of the carbonization chamber. At the same time, measurements in the width direction are performed by the individual sensors 1, and individual measured values L1, L2, L3,... are obtained. Then the extruder is advanced, the rod 3 is moved by a distance between correction sensors 8, 9, and a distance t up to the oven wall 6 is measured by the sensor 9 in a state that the rod 3 has been deformed thermally. At this time, the criterion value t1 is regarded as having been changed by (t1-t2)=DELTAt. When the worn-out amount of the oven wall is found, it is corrected by DELTAt. When measured values by the individual sensors 1 at this time are designated as M1, M2, M3,..., worn- out amounts.of the oven wall are M1-t1+DELTAt, M2-t1+DELTAt, M3-t1+DELTAt,....
    • 6. 发明专利
    • PRODUCTION OF FORMED COKE
    • JPH06330046A
    • 1994-11-29
    • JP11963193
    • 1993-05-21
    • KAWASAKI STEEL CO
    • OSADA YASUSHIAIHARA TSUNEOIMAIZUMI FUJIO
    • C10B3/02C10B53/08C10B57/04C10B57/10
    • PURPOSE:To efficiently obtain formed coke by heating part of the coke oven gas produced in a dry distillation oven with a continuous heat exchanger and returning the gas to the oven and by using the combustion exhaust gas generated as heat source for adjusting moisture content of coal to effect energy saving. CONSTITUTION:A dryer 2 is fed with coal 1 which is, in turn, fed with the combustion exhaust gas 14 at 250-300 deg.C generated from a continuous heat exchanger 10 to adjust moisture content of the coal 1, and the exhaust gas 27 passed through the dryer 2 is freed from dust using a dust remover 26 and the resultant exhaust gas 28 is released via a stack 13 into the air. The moisture-adjusted coal is then regulated in granular size with a grinder 3, being kneaded with a binder 20 and hot water 21 using a kneader 4 and made into formed coal 12 with a molding machine 5. Subsequently, the formed coal 12 is loaded in a dry distillation oven 6, being heated directly with hot air 24, 25 to conduct dry distillation to produce formed coke 7 which is then discharged via the oven bottom out of the oven. For the hot air 24, 25 for dry distillation, part of the coke oven gas 16 generated in the dry distillation oven 6 is heated with a high-temperature gas heater 11 and further heated with the continuous heat exchanger 10 and then returned to the dry distillation oven 6.
    • 9. 发明专利
    • SLAG-TREATING EQUIPMENT IN BLAST FURNACE
    • JPH0492840A
    • 1992-03-25
    • JP20600490
    • 1990-08-03
    • KAWASAKI STEEL CO
    • NIKO KIYOSUKEAIHARA TSUNEOHASEGAWA TSUNEYA
    • C04B5/00
    • PURPOSE:To obtain a treating equipment having excellent solid-liquid separating function with a miniature size by discharging granulated slurry stored in a storing tank in an equipment performing granulating treatment of molten slag with separating to solid and liquid with a net conveyer having a bucket. CONSTITUTION:Molten slag from a blast furnace is introduced into a stirring tank 2 through a slag gutter 1 and made to granulated slurry with cooling by high-pressure water jetted from a blowing box 6, then sent to a settling tank 8 to be settled under the water surface. The settled granulated slag is scooped in buckets on a net conveyer 10 and upwardly transferred, then the granulated slag in the bucket is separated to solid and liquid through a conveyer belt 15 made of a metal net, thus stored in a product tank. On the other hand, water is taken out from a water-takeout part 23 inhibiting invasion of the granulated slag from a side face-side with sealing part materials 25a and 25b attaching to both side parts of whole region from upper side of the water surface to submerged region under water in the settling tank 8 containing the conveyer 10. Thereby, water having high clarity can be recovered through a filter using the belt 15.