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    • 1. 发明专利
    • OPERATION CONTROL METHOD OF COAL GASIFIER OVEN
    • JPS63264696A
    • 1988-11-01
    • JP9810587
    • 1987-04-21
    • HITACHI LTDBABCOCK HITACHI KK
    • TOMURO JINICHITANAKA SHINJIMORIHARA ATSUSHIMATSUO MITSUHIROSUGITA NARIHISANOGUCHI YOSHIKI
    • C10J3/46C10J3/86
    • PURPOSE:To control the temp. of a gasifier oven irrespective of a wide load variation range so as to obtain a product gas of constant calorific value, by compensating for an oven temp. decreases occurring in the stage of low load in a entrained bed type coal gasifier oven by elevation of the preheating temp. of a gasifying agent. CONSTITUTION:Coal 1 is fed into a coal gasifier oven 10 through a flow rate regulator 2. A gasifying agent 41, such as air, is fed through a flow rate regulator 42, controlled with signal 57 converted from the signal 56 of the regulator 2 by the use of a control operation unit 3, into a heat exchange 36 wherein preheating is conducted. The preheated gasifying agent 44 is fed into the oven 10, wherein the coal 1 is partially oxidized. The ash is melted and discharged as slag 17, and the crude product gas 11 is cooled by a cooler 12 and fed into a purifier apparatus 14, wherein dedusting and desulfurization are conducted. Most portion of the purified gas 15 is taken out as combustion gas 16. Portion of the combustion gas is extracted as a fuel 21 for gasifying agent preheating, and fed through a flow rate regulator 22. controlled with the temp. signal 51 of the combustion waste gas 37 discharged from the heat exchanger 36, into the oven 10 and a combustor 30 to which the air 31 controlled with the temp. signals 53, 54, 55 of the gasifying agent44 and high temp. combustion gas 35 is introduced. In the combustor, combustion is conducted. The high temp. combustion gas thus formed is fed to the heat exchange 36, wherein the gas is used to preheat the gasifying agent 43.
    • 2. 发明专利
    • Stabilized dust coal feeder
    • 稳定的煤炭进料器
    • JPS6191293A
    • 1986-05-09
    • JP21135984
    • 1984-10-11
    • Babcock Hitachi KkHitachi Ltd
    • KOYAMA SHUNTAROMIYAMOTO TOMOHIKOMATSUO MITSUHIROTANAKA SHINJIMORIHARA ATSUSHI
    • C10J3/72C10J3/50
    • PURPOSE: To feed dust coal with a high reliability under a stabilized condition, by detecting abnormality in a dust coal supply system and, once abnormality has occurred, blowing a high-pressure gas into the system to restore the original state.
      CONSTITUTION: Dust coal 1 is placed in a hopper 4 and fed by a feeder 5 to a coal/carrier gas confluence zone 6. The dust coal is carried by the carrier gas 2 to a coal distributor 7 through a pipe 20 and sent to a gasifying oven 9 through a pipe 21. Differential pressure gages ΔPa:10 are attached to an outlet of the feeder 5 and an inlet of the distributor 7, differential pressure gages ΔPb
      1W4 :11, to the inlet and outlet of the distributor 7 and differential pressure gages ΔPc
      1W4 :12, to piping between the outlet of the distributor 7 and an entrance of the oven 9. A valve 13 is attached to the pipe 29, valves 14W17, to the pipe 21 and valves 18aW18d, to an outlet of a high-pressure tank 8. Signals from the differential pressure gages 10W12 are put in a control unit 30 and, when abnormality has occurred, one of the valves 18aW18d is opened momentarily to feed a high-pressure gas 3 intermittently for removal of deposits in the supply system.
      COPYRIGHT: (C)1986,JPO&Japio
    • 目的:在稳定的条件下,通过检测粉煤供应系统的异常情况,在稳定的条件下,以高可靠性喂粉尘煤,一旦发生异常,将高压气体吹入系统恢复原状态。 构成:灰尘煤1放置在料斗4中,并通过进料器5供给到煤/载气汇合区6.粉尘煤由载气2通过管道20运送到煤分配器7,并送到一个 差压压力计DELTAPa:10连接到进料器5的出口和分配器7的入口,压差计DELTAPb1-4:11,分配器7的入口和出口以及 压差计DELTAPc1-4:12分配给分配器7的出口和烘箱9的入口之间的管道。阀13连接到管道29,阀门14-17,管道21和阀门18a-18d 到高压罐8的出口。来自差压计10-12的信号放在控制单元30中,并且当异常发生时,阀18a-18d中的一个暂时打开以供给高压罐8。 压力气体3间歇地用于去除供给系统中的沉积物。
    • 3. 发明专利
    • Apparatus for drawing out coal ash slag
    • 用于绘制煤灰浆的装置
    • JPS59206490A
    • 1984-11-22
    • JP8075883
    • 1983-05-11
    • Babcock Hitachi KkHitachi Ltd
    • YAHAGI TOSHIONOKITA SHIYUNSUKEKOYAMA SHIYUNTAROUTOMURO JINICHIMORIHARA ATSUSHIMATSUO MITSUHIROMIYADERA HIROSHI
    • C10J3/46
    • PURPOSE: To keep the calorific value of the produced gas constant even during the fluctuation of load and to prevent a slag discharge port from being clogged without lowering gasification efficiency, by embedding an electric resistance-heating unit in the area of a molten slag discharge port.
      CONSTITUTION: Pulverized coal 21 and oxygen 22 are fed to a gasifying chamber 1 and partially burnt to gasify the coal 21 while keeping the temp. at a level not lower than the melting temp. of ash contained in the coal, and the produced gas 23 is recovered from the upper part. Ash contained in the coal 21 is allowed to flow in a molten state through a slag discharge port 2 into a cooler 3 to cool and solidify it with cooling water 24. A coil heating unit 8 is embedded in the slag discharge port 2, and a lead wire 9 is connected to both terminals of the heating unit 8. The temp. of the slag discharge port 2 is controlled to a temp. not lower than the m.p. of the ash in the coal by the heating unit 8, whereby molten slag is prevented from being solidified on the way of the slag discharge port 2.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:为了在负载波动期间保持产生的气体的发热量恒定,并且在不降低气化效率的情况下防止排渣口堵塞,通过将电阻加热单元嵌入熔渣排出口的区域 。 构成:粉煤21和氧22被送入气化室1并部分燃烧以使煤21气化,同时保持温度。 处于不低于熔融温度的水平。 煤中所含的灰分,从上部回收生成气体23。 允许煤21中含有的灰分通过排渣口2流入冷却器3,以冷却水24冷却固化。线圈加热单元8嵌入排渣口2中, 引线9连接到加热单元8的两端。 的排渣口2被控制在温度 不低于m.p. 的煤通过加热单元8的灰分,从而防止熔渣在渣排出口2的途中固化。
    • 4. 发明专利
    • BRANCHED CONVEYING PIPE FOR POWDERED COAL
    • JPS5982227A
    • 1984-05-12
    • JP19248382
    • 1982-11-04
    • HITACHI LTDBABCOCK HITACHI KK
    • MORIHARA ATSUSHIKOYAMA SHIYUNTAROUMATSUO MITSUHIRO
    • B65G53/52C10L5/00
    • PURPOSE:To perform the uniform distribution of powdered coal subject to pneumatic conveyance in a simple structure, by installing a stagnant region in the terminal part of a vertically upward conveying pipe, while connecting plural horizontal conveying pipes to the lower part of the said region via a small diametral part. CONSTITUTION:In case of a device, using nitrogen or the like as a conveying gaseous body, that pneumatically conveys powdered coal to a branched conveying device 7 from a conveying pipe and uniformly conveys the powdered coal to a coal gasifier furnace or the like from the said device 7 after being plurally dispersed, the branched conveying device 7 is composed of a straight pipe conveying part 10, a branched part 11 at the terminal of the said conveying part 10, and plural horizontal conveying part 13 installed extendedly toward a right-angled direction to this branched part 11. At this time, the diameter of a junction part with the straight pipe conveying part 10 of the plural horizontal conveying part 13 is made to be thined as compared with that of the horizontal conveying part 13. In addition, a stagnant part 12 is installed in the more upper traight pipe conveying part than the said junction part. With this method, a mixed stream 14 of the powdered coal and the conveying gaseous body is led into the stagnant part 12 and, after being turned over hereat, led into the horizontal conveying part 13 so that uniform dispersion can be thus attained.
    • 5. 发明专利
    • METHOD AND DEVICE FOR MEASURING POWDER FLOW RATE BY ATTENUATION OF SOUND WAVE
    • JPS63138214A
    • 1988-06-10
    • JP28434786
    • 1986-12-01
    • HITACHI LTDBABCOCK HITACHI KK
    • MORIHARA ATSUSHIMATSUO MITSUHIROKOYAMA SHUNTARO
    • G01F1/712
    • PURPOSE:To execute an exact measurement which is excellent in its responsiveness, by calculating a powder flow rate from the product of a powder concentration calculated by measuring an attenuation of a sound wave by powder, and a powder speed calculated by measuring a delay time between measuring points. CONSTITUTION:Powder 70 is carried by passing through the inside of a carrying pipe 80. A sound wave generator 11 generates a sound wave between 1kHz and 1kHz, and this sound wave is emitted to the inside of the carrying pipe 80 by a sound wave element 12. The emitted sound wave is attenuated due to existence of the powder 70 and reaches a sound wave element 22. The sound wave transmitted to the element 22 is detected by a sound wave detector 21, and converted to a powder concentration by a concentration detector 31. The same measurement is executed between the elements 11, 12 and sound wave elements 14, 24 separated in the flow direction of the powder 70, as well. Results of detection of detectors 31, 32 are sent to a powder average flow rate calculator 60 through an average concentration calculator 40 and a speed computing element 50. In such a way, the measurement of a powder flow rate, which is excellent in its responsiveness can be executed.
    • 6. 发明专利
    • Method for gasifying coal
    • 燃煤的方法
    • JPS59206488A
    • 1984-11-22
    • JP8075583
    • 1983-05-11
    • Babcock Hitachi KkHitachi Ltd
    • TOMURO JINICHIKOYAMA SHIYUNTAROUMORIHARA ATSUSHIMATSUO MITSUHIROMIYADERA HIROSHI
    • C10J3/46
    • PURPOSE: To provent the clogging of an ash-discharge port under a low load operation, by partially oxidizing coal with oxygen or an oxygen-contg. gas to gasify the coal and feeding oxygen or an oxygen-contg. gas through a molten ash-discharge port in the opposite direction from the flow of molten ash.
      CONSTITUTION: Pulverized coal 21 and oxygen or an oxygen-contg. gas 21 are fed through a nozzle 11 to a gasifying chamber 1 and partially burnt to thereby convert it into a combustible gas which is then recovered as the produced gas from the upper part. Ash contained in coal is molten by heat generated by partial combustion, allowed to drop through a slag tap 2 into a cooler 12 to cool and solidity it with a cooling water 25 and withdrawn from a valve 14. Oxygen or an oxygen-contg. gas 24 from the upper part of the cooler 12 is fed to a space between the slag tap 2 and the cooling water 25 to burn combustible gas in the neighborhood of the slag tap 2, whereby the slag tap 2 is kept at a high temp. by generated heat to prevent clogging caused by the solidification of slag.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:为了防止在低负荷作业下灰渣排出口的堵塞,通过用氧气或氧气接触部分氧化煤。 气体气化煤和供氧或氧气。 气体通过熔融灰渣排出口与熔融灰流相反的方向。 构成:粉煤21和氧气或氧气。 气体21通过喷嘴11供给到气化室1并部分燃烧,从而将其转化为可燃气体,然后从上部回收作为产生气体的可燃气体。 包含在煤中的灰被部分燃烧产生的热量熔化,允许通过炉渣丝锥2落入冷却器12中,以冷却水25冷却并固化,并从阀门14排出。氧气或氧气不足。 将来自冷却器12的上部的气体24供给到炉渣排出口2和冷却水25之间的空间,以将炉渣2附近的可燃性气体燃烧,从而将渣渣2保持在高温。 通过产生的热量来防止由渣固化引起的堵塞。
    • 7. 发明专利
    • Gasification of coal
    • 煤气化
    • JPS59172589A
    • 1984-09-29
    • JP4716283
    • 1983-03-23
    • Babcock Hitachi KkHitachi Ltd
    • KOYAMA SHIYUNTAROUMORIHARA ATSUSHIMATSUO MITSUHIROMIYADERA HIROSHITOMURO JINICHINOGUCHI YOSHIKI
    • C10J3/46
    • PURPOSE: To gasify coal efficiently, by feeding raw material dust coal to two burners in different gasification reaction zones of a gasifying oven and controlling the feed ratio of oxygen to dust coal to a specific value.
      CONSTITUTION: Raw material dust coal 1 is divided into two lots, which are fed separately into a gasification reaction zone 30 of a gasifying oven through an upper burner 27 and a lower burner 28. The feed ratio of oxygen to dust coal in the upper burner 27 is set at such a value that the temperature near the upper burner 27 may not exceed the fusion temperature of dust coal ash and that of oxygen to dust coal in the lower burner 28 is set higher than that in the upper burner 27 and the temperature near the lower burner 28 is raised to above the fusion temperature of ash. Gas produced in the lower zone and containing CO
      2 , H
      2 O, etc. is made to react as gasifying agent with highly reactive char produced in the upper zone to effect gasification of the char.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:通过在煤气化炉的不同气化反应区内将原料粉尘煤送入两台燃烧器,将氧气和粉尘煤的进料比控制在一定的范围内,有效地将煤气化。 构成:原料粉煤1分为两批,分别通过上燃烧器27和下燃烧器28供给到气化炉的气化反应区30中。上燃烧器中氧与灰煤的供料比 27设定为使得上燃烧器27附近的温度不能超过下燃烧器28中的灰尘煤灰和氧气对灰尘的熔化温度设定为高于上燃烧器27的温度和温度 在下燃烧器28附近被升高到高于灰分的熔融温度。 在下部区域产生的含有CO 2,H 2 O等的气体作为气化剂与在上部区域产生的高反应性焦炭反应以实现炭的气化。
    • 10. 发明专利
    • Coal gasifying oven
    • 煤炭气化炉
    • JPS59176391A
    • 1984-10-05
    • JP5049683
    • 1983-03-28
    • Babcock Hitachi KkHitachi Ltd
    • MORIHARA ATSUSHIKOYAMA SHIYUNTAROUMATSUO MITSUHIROMIYADERA HIROSHITOMURO JINICHINOKITA SHIYUNSUKENOGUCHI YOSHIKIHISHINUMA TAKAO
    • C10J3/46C10J3/48
    • C10J3/466C10J3/485C10J3/487C10J2300/093C10J2300/0959C10J2300/1846Y10S48/04
    • PURPOSE: To increase the efficiency of gasification of coal in a coal gas liquefaction apparatus which employs a double jet layer, by reducing the diameter of a discharge opening and providing two specially designed burners to the reactor wall.
      CONSTITUTION: A produced gas discharge opening 2 and a slag discharge opening 11 having a diameter smaller than that of a gasification reaction zone 8 formed in a container 3 (4 is heat insulating material) are provided at the top and bottom of the gasification reaction zone 8 respectively. Upper burners 7, 7 and a lower burner 9 for introduction of dust coal and a gasifying agent are attached to the wall of the container 3 (and the heat insulating material 4) so that dust coal, etc. may be blown in a tangential direction to imaginary circles A and B assumed in the gasification reaction zone 8 and the imaginary circle A for the upper burner 7 may have a diameter larger than that of the imaginary circle B for the lower burner 9 (13 is a layer of water to cool discharged slag; 12 is an inlet for cooling water; 14 is an outlet for cooling water).
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:通过减小排放口的直径,并向反应器壁提供两个特别设计的燃烧器,提高采用双层喷射层的煤气液化装置中煤的气化效率。 构成:在气化反应区域的顶部和底部设置有形成在容器3(4为绝热材料)中的气化反应区8的直径小于直径的产生气体排出口2和排渣口11 8。 上部燃烧器7,7和用于引入粉尘煤和气化剂的下部燃烧器9附接到容器3(和隔热材料4)的壁上,使得灰尘等可以沿切线方向吹 在气化反应区8中假设的假想圆A和B以及用于上部燃烧器7的假想圆A的直径可以比下部燃烧器9的假想圆B的直径大(13是一层水冷却排出 炉渣; 12是用于冷却水的入口; 14是用于冷却水的出口)。