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    • 91. 发明专利
    • CONTROLLER FOR WET TYPE WASTE GAS DESULFURIZING DEVICE
    • JPH038410A
    • 1991-01-16
    • JP14226389
    • 1989-06-06
    • BABCOCK HITACHI KK
    • KATSUBE TOSHIONOZAWA SHIGERUNAKAMOTO TAKANORIEGASHIRA MICHIOMASUTOMI HIROSHIKAMOGAWA HIROMI
    • B01D53/50B01D53/34B01D53/77
    • PURPOSE:To stop unnecessary pumps without impairing the performance of the wet type exhaust gas desulfurizing device for boilers for intermediate load operation with which the frequencies of start and stop are many by allowing the number of the circulating pumps to be controlled according to the operating conditions of the plant even with the above-mentioned wet type waste gas desulfurizing device. CONSTITUTION:Absorption liquids are supplied by plural units of the circulating pumps to an absorption column which absorbs away the SOX in waste gases. The number of the pumps to be operated is controlled according to the load. Operation history signals 14 of the circulating pumps, start limit condition signals 15 of the circulating pumps, intended load signals 16 of the absorption column, and SOX signals 17 in the waste gases are inputted and outputted in a data input/output section 18 in the controller. Desulfurizing performance is computed from the signals 16, 17 in a section 19 for computing the desulfurizing performance. Further, the required number of the circulating pumps to be operated is computed in accordance with the signals 16, 17 in a section 20 for computing the required flow rate of the circulating liquid. The pumps are selected from the computed number of the pumps to be operated and the signals 14, 15 in a section 21 for deciding the okay or not of pump stop. The start and stop of the pumps are executed by a control section 22.
    • 92. 发明专利
    • APPARATUS FOR WET DESULFURIZATION OF EXHAUST GAS
    • JPH01236923A
    • 1989-09-21
    • JP6456588
    • 1988-03-17
    • BABCOCK HITACHI KK
    • KATSUBE TOSHIONAKAMOTO TAKANORI
    • B01D53/50B01D53/34B01D53/77
    • PURPOSE:To keep the concn. of Cl const. in discharged water of desulfurization to be processed by a wastewater treating apparatus, by estimating the concn. of Cl in the discharged water on real time from the conditions of a boiler and a desulfurizing apparatus and adjusting the supplying amount of the discharged water of desulfurization according to the concn. of Cl. CONSTITUTION:The total flow amount of Cl is calculated by a multiplier and an adder by sending the signals from a detector 50 of the flow amount of a discharge gas flowing before a desulfuring apparatus 5, a detector 51 of Cl concn. in the discharged gas, a detector 52 of water-supplying amount of a water supplying line 19 to a thickener over-flow water tank 18, and a detector 53 of Cl concn. in the supplied water. Meanwhile, the total discharged water amount is calculated from the signals from a detector 56 of the flow amount of an adsorbing agent slurry and a detector 55 of the discharged water flow amount. From the both, Cl concn. in the discharged water is calculated, compared with the set value, and by the resulting deviation signal, a valve 54 to adjust the discharged water flow amount is controlled so as to control the flow amount of the discharged water of desulfurization into a wastewater treating apparatus.
    • 93. 发明专利
    • Wet stack gas desulfurizer
    • 湿堆积气体脱硫剂
    • JPS6182826A
    • 1986-04-26
    • JP20256084
    • 1984-09-27
    • Babcock Hitachi Kk
    • KATSUBE TOSHIO
    • B01D53/50B01D53/34B01D53/77
    • PURPOSE: To accelerate the dissolution velocity of limestone without increasing the amt. of circulating liq. in an absorption tower and without increasing the excess rate of the limestone and to restore the pH of a liq. absorbent by providing the second liq. absorbent storage vessel which is connected to a liq. absorbent storage vessel in an absorption tower and whose liq. surface is brought into contact with air.
      CONSTITUTION: A partition plate 30 having the communicating part of a liq. absorbent at the lower part is provided to a liq. absorbent storage vessel 20 of an absorption tower 4, and the second liq. absorbent storage vessel 21 whose gaseous-phase part is isolated from waste gas is furnished. The liq. absorbent after absorbing SO
      2 in waste gas is firstly stored in the first liq. absorbent storage vessel 20, and then sent into the storage vessel 21 from the communicating part at the lower part of the parti tion 30. The gaseous phase at the upper part of the second storage vessel 21 is isolated from CO
      2 -rich waste gas, and brought into contact with the atmosphere having low CO
      2 content. Accordingly, decarbonation reaction proceeds, and the dissolution velocity of limestone is accelerated. The liq. absorbent whose pH is restored in the second storage vessel 21 is supplied to the absorption tower 4 by a pump 11. The gaseous CO
      2 evolved in the storage vessel 21 is discharged into the absorption tower 4 by a pipeline 24.
      COPYRIGHT: (C)1986,JPO&Japio
    • 目的:加快石灰石的溶解速度,不增加灰分。 的循环流程 在吸收塔中,并且不增加石灰石的过剩率并恢复液体的pH。 通过提供第二液体吸收剂。 连接到液体的吸收性储存容器。 吸收塔中的吸收性储存容器。 表面与空气接触。 构成:具有连接部分的隔板30。 吸收剂在下部被提供到液体。 吸收塔4的吸收性储存容器20,以及第二液体。 提供其气相部分与废气隔离的吸收性储存容器21。 liq。 吸收废气中的二氧化硫后的吸收剂首先储存在第一液体中。 吸收性储存容器20,然后从第二部分30的下部的连通部分送入储存容器21.第二储存容器21上部的气相与富含CO 2的废气分离, 与具有低CO 2含量的气氛接触。 因此,脱碳反应进行,石灰石的溶解速度加快。 liq。 在第二储存容器21中恢复pH的吸收剂通过泵11供应到吸收塔4.在储存容器21中放出的气态CO 2通过管线24排出到吸收塔4中。
    • 94. 发明专利
    • Control of wet waste gas desulfurization apparatus
    • 湿废气脱硫装置的控制
    • JPS59169523A
    • 1984-09-25
    • JP4141683
    • 1983-03-15
    • Babcock Hitachi Kk
    • NARITA TSUNEONISHIMURA TSUCHIKATSUBE TOSHIOASANO HIROMITSUOBATA KOUZOUSOGA MITSUSACHI
    • B01D53/50B01D53/34B01D53/77C01F11/46
    • PURPOSE: To attain to reduce the power cost of an air compressor, by controlling the amount and pressure of air supplied to an oxidizing tower corresponding to the amount of calcium sulfite generated in an exhaust gas absorbing tower supplied to the oxidizing tower.
      CONSTITUTION: In a wet waste gas desulfurization by absorbing SO
      x in exhaust gas with a limestone slurry is supplied to an oxidizing tower 15 through an oxidizing tower supply tank 13 to be oxidized to calcium sulfate with air sent into said tower 15 from an oxidizing air compressor 21 while the reaction mixture is withdrawn to a gypsum thickener 16 to recover gypsum, the air amount sent to the oxidizing tower 15 is controlled corresponding to the amount of calcium sulfite supplied to said oxidizing tower 15 by a flow meter 105 and a control valve 111 or air pressure is controlled by a pressure controller 107 and a control valve 110. In parallel to this operation, a suction valve 113 and an air release valve 112 are opened and closed by the pressure switch 106 provided to an air tank 22 for storing oxidizing air to subject the air compressor 21 to repeated load and unload operations and the power reduction during low load is performed.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:为了降低空气压缩机的动力成本,通过控制供给氧化塔的空气的量和压力,与供给氧化塔的废气吸收塔中产生的亚硫酸钙的量相对应。 构成:在通过用石灰石浆料吸收废气中的SO x的湿废气中,通过氧化塔供应罐13将氧化塔15供给到氧化塔15中,以从氧化空气压缩机送入塔15的空气被氧化成硫酸钙 21,同时将反应混合物取出到石膏增稠剂16中以回收石膏,送入氧化塔15的空气量通过流量计105和控制阀111对应于供给到氧化塔15的亚硫酸钙的量来控制 或气压由压力控制器107和控制阀110控制。与此同时,吸入阀113和排气阀112被设置在用于储存氧化的空气罐22的压力开关106打开和关闭 空气对空气压缩机21进行重复的负载和卸载操作,并且执行低负载期间的功率降低。
    • 96. 发明专利
    • Shot cleaning apparatus and its operation method
    • SHOT CLEANING装置及其操作方法
    • JP2003075093A
    • 2003-03-12
    • JP2001269434
    • 2001-09-05
    • Babcock Hitachi Kkバブコック日立株式会社
    • MURAMOTO KOJISAITO TAKAYUKIMIYATAKA RYOICHIKATSUBE TOSHIOOKAWA TAKESHITAWARA HISATO
    • F28G1/12F28G15/04
    • PROBLEM TO BE SOLVED: To provide a shot cleaning apparatus and its operation method, in which a flow rate of shots of steel balls is easily variable in response to load change or increase of pressure loss in a GGH (gas-gas heater) without upsizing the apparatus.
      SOLUTION: Dust adhered to heat transfer pipes 5 is removed by scattering shots from a feeder 1 on the pipes 5 which performs heat exchange between the inner fluid and dust-containing gas. Shot circulation in the apparatus is controlled by varying the shot-transfer speed of the feeder 1 by employing a controllable motor, e.g. provided with an inverter. The shots are spontaneously dropped all the time as required from a bypass chute 11 provided in the feeder 1. Further, a specified amount of shots are added all the time from a feeder 10 of a shot tank 9 in the outside of the system to the shot circulation system. In this case, operation is kept in a constant speed (maximum capacity) in the shot-transfer system including a shot-transferring bucket-conveyor 8, a shot distributor 4, a dust separator 6 and a shot discharger 7, etc.
      COPYRIGHT: (C)2003,JPO
    • 要解决的问题:提供一种喷丸清理装置及其操作方法,其中钢球的喷射流量响应于GGH(气体加热器)中的负载变化或压力损失的增加而容易变化,而不增大 该装置。 解决方案:通过在进行内部流体和含尘气体之间的热交换的管道5上的进料器1的散射射流来消除附着在传热管5上的灰尘。 通过采用可控制的电动机,例如通过改变进料器1的射出传送速度来控制装置中的喷射循环。 配有变频器。 根据需要,从投放机1中设置的旁路槽11自发地投射投射。此外,从系统外部的喷射槽9的进料器10一直加入规定量的喷射量 射击循环系统 在这种情况下,在包括射出转移斗式输送机8,射击分配器4,灰尘分离器6和射出放出器7等的射出传送系统中,操作保持恒定的速度(最大容量)。