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    • 1. 发明专利
    • PREPARATION OF PLAN FOR TAKING OUT COKE, AND APPARATUS THEREFOR
    • JPH10292176A
    • 1998-11-04
    • JP10207397
    • 1997-04-18
    • FUJITSU LTDNIPPON KOKAN KK
    • MATSUMOTO SHUNJIYAMAMOTO SHUICHITAKETOMI HIROFUMIEBIHARA TAMEFUMI
    • C10B33/00C10B41/00C10B57/00
    • PROBLEM TO BE SOLVED: To provide a method for preparing a plane for taking out coke for a plurality of coke ovens operated while being separated into a prescribed number of series according to the kind of cokes to be produced by which the need for knowledge acquiring operations can be eliminated to avoid such conditions that nothing is known at all until a solution is obtained, and practice is stopped at a suitable time and operations can be performed by using the best solution at the time as an actually adaptable one, and also an apparatus therefor. SOLUTION: Prescribed conditions for preparing a plan are inputted to produce operation blocks for successively operate pushers for charging coke into ovens for the coke with the first genetic algorism(GA) based on the conditions for preparing the plan and the arrangement order of the operation blocks is optimized to optimize the starting time in the allocatable time of the operation blocks in which the sequential order is optimized with the second GA. The operation blocks in the allocatable time are displayed for each series and a plan for pushing the coke, as necessary corrected, is transmitted to a computer for control capable of controlling the oven for the coke in the method for preparing the plan for pushing the coke comprising preparing the plan for pushing of the plural ovens for the coke operated in divisions into a prescribed number of series according to the kind of the produced coke.
    • 4. 发明专利
    • METHOD FOR CHARGING COAL INTO COKE OVEN
    • JPH0356587A
    • 1991-03-12
    • JP19371489
    • 1989-07-26
    • NIPPON KOKAN KK
    • NAKAJIMA RYUICHIHASEBE SHINJITAKETOMI HIROFUMI
    • C10B31/00C10B41/00
    • PURPOSE:To eliminate a partial excess and insufficient amount of charging coal and defective carbonization only and reduce heat quantity basic unit by determining average temperature between respective sections from measured values of oven wall temperatures of coke oven carbonization chambers and correcting the amount of the charging coal in the aforementioned sections. CONSTITUTION:Coke in each carbonization chamber 1 is discharged with a pusher. In the process, the upper, middle and lower temperatures of the oven wall are measured with a radiation type thermometer 4 provided in a ram head 3 and the resultant values are transmitted to the central arithmetic unit 5 where the average values of the oven wall temperatures of the respective sections are calculated. A correction coefficient of the amount of charging coal in the respective sections is calculated based on a difference between the average values and the previously inputted target temperatures of the respective sections to determine the actual amount charged, which is then transmitted to an automatic coal charging unit of a coal charging cart. The coal is charged from the respective coal charging ports 21, 22, 23 and 24 into the respective carbonization chambers while measuring the coal with a hopper scale of the coal charging cart. When the amount attains a prescribed value, a mining feeder is automatically stopped.
    • 5. 发明专利
    • METHOD FOR ESTIMATING MAXIMUM FLUIDITY COMBINED COAL
    • JPH0220592A
    • 1990-01-24
    • JP17056988
    • 1988-07-08
    • NIPPON KOKAN KK
    • KATO TOMONORIFUNABIKI YOSHIHIROTAKETOMI HIROFUMI
    • C10B57/04
    • PURPOSE:To enable the production of a coke having a desired high strength by obtaining the logarithmic value of the flow temp. for each coal to be combined at each predetermined temp. between the flow initiating temp. and the solidifying temp., calculating weighted averages from the values to obtain the fluidities of combined coal and presuming the max. thereof as the max. fluidity of combined coal. CONSTITUTION:The flow curve for each coal to be combined is enciphered from the flow initiating temp., max. flow temp., solidifying temp. and fluidity thereof, thereby obtaining a numerical formula. On the basis of this formula, the logathmic value of the fluidity for each coal to be combined at each predetermined temp, between the flow initiating temp. and the solidifying temp. is calculated. Weighted averages are calculated from the resultant logathmic values of the fluidity to obtain the fluidities of combined coal. The max. of the obtd. fluidities of combined coal is presumed as the max. fluidity of combined coal. The above method enables the estimation of the max. fluidity accurately. As a result, it is possible to produce a coke having a desired high strength.
    • 10. 发明专利
    • BENT RISER OF COKE OVEN
    • JPH03210386A
    • 1991-09-13
    • JP562990
    • 1990-01-12
    • NIPPON KOKAN KK
    • OSHIMA YOSHIHIROHASEBE SHINJITAWARA TSUTOMUTAKETOMI HIROFUMI
    • C10B27/06
    • PURPOSE:To prevent pitch and carbon produced from generated gas from adhering to thereby dispense from the removal of carbon by coating the inner wall of a bent part of a bent riser with a wall release material and providing means for jet-cooling the inner wall. CONSTITUTION:A gas at a high temperature of about 800 deg.C which is generated from an opening 3 of the top of a coke oven is passed through a riser 1 and then through a bent part 22 and a vertical part 23 of a bent riser 21. Herein a cooling water from an annular slit nozzle 27 provided at an inlet end of the bent part 22 is jetted against the inner wall coated with a wall release material comprising a graphite coating material or a synthetic fluororesin in such a manner that the cooling water does not enter the riser 1, thereby cooling the inner wall to 300 deg.C or below. Then, even if pitch and carbon are produced from the generated gas, they do not adhere to the surface of the wall release material 24 and are washed away into the vertical part 23 by the jetted cooling water.