Neutralization method and neutralization plant

    公开(公告)号:US09752211B2

    公开(公告)日:2017-09-05

    申请号:US14382737

    申请日:2013-03-01

    CPC classification number: C22B23/0461 C22B3/04 C22B23/0423 Y02P10/234

    Abstract: A method for improving the filterability in separating a zinc sulfide, produced by applying sulfurization treatment to a post-neutralization solution containing zinc together with nickel and cobalt in a dezincification step in a hydrometallurgical process for nickel oxide ore. The method includes a neutralization reaction step of neutralizing leachate in a neutralization tank, a separation step of separating neutralized slurry into a neutralized sediment and a post-neutralization solution by adding flocculant to the neutralized slurry, a measuring step of measuring the viscosity of the post-neutralization solution, a step of storing the post-neutralization solution in a storage tank, and a transfer step of transferring the stored post-neutralization solution to a dezincification reaction tank used in a dezincification step subsequent to a neutralization step.

    Hydrogen sulfide gas production plant system and method for recovering and using hydrogen sulfide gas
    4.
    发明授权
    Hydrogen sulfide gas production plant system and method for recovering and using hydrogen sulfide gas 有权
    硫化氢气体生产厂系统及回收利用硫化氢气体的方法

    公开(公告)号:US09321646B2

    公开(公告)日:2016-04-26

    申请号:US14416428

    申请日:2013-07-08

    Abstract: The present invention allows low-concentration hydrogen sulfide gas to be recovered and supplied to a processing plant that uses hydrogen sulfide gas. The hydrogen sulfide gas production plant is provided with a first supply pipe that supplies hydrogen sulfide gas obtained from a sulfur recovery facility to a processing plant, and a second supply pipe that is branched at a predetermined point in the first supply pipe and supplies the hydrogen sulfide gas from the sulfur recovery facility to the processing plant. The first supply pipe has a concentration meter that is provided on the upstream side than the branch point and measures the concentration of the hydrogen sulfide gas. The first supply pipe and the second supply pipe have ON/OFF valves that are provided on the downstream side of the branch point and perform ON/OFF control of the supply to the processing plant through the supply pipe.

    Abstract translation: 本发明允许回收低浓度硫化氢气体并将其供给到使用硫化氢气体的处理厂。 硫化氢气体生产设备设置有将从硫回收设备获得的硫化氢气体提供给处理设备的第一供应管道和在第一供应管道中的预定点处分支并供应氢气的第二供应管道 从硫回收设施到加工厂的硫化物气体。 第一供给管具有设置在比分支点上游侧的浓度计,并测量硫化氢气体的浓度。 第一供给管和第二供给管具有设置在分支点的下游侧的开关阀,并且通过供给管进行对加工厂的供给的ON / OFF控制。

    HYDROGEN SULFIDE GAS PRODUCTION PLANT AND METHOD FOR RECOVERING AND USING WASTE HYDROGEN SULFIDE GAS
    5.
    发明申请
    HYDROGEN SULFIDE GAS PRODUCTION PLANT AND METHOD FOR RECOVERING AND USING WASTE HYDROGEN SULFIDE GAS 有权
    硫化氢气体生产设备和废水回收和使用硫化氢气体的方法

    公开(公告)号:US20150044126A1

    公开(公告)日:2015-02-12

    申请号:US14371474

    申请日:2013-01-07

    CPC classification number: B01J7/00 B01J2219/00002 C01B17/162 C01B17/168

    Abstract: An object is to provide a hydrogen sulfide gas production plant that can recover discharged waste hydrogen sulfide gas and efficiently supply the gas to a process plant where processing is conducted by using hydrogen sulfide gas, and also provide a method for recovering and using the waste hydrogen sulfide gas by the hydrogen sulfide gas production plant. In the present invention, the hydrogen sulfide gas production plant is provided with a pipe that recovers the waste hydrogen sulfide gas discharged from the hydrogen sulfide gas production plant and that has one end connected to the process plant where the hydrogen sulfide gas is used, and the discharged waste hydrogen sulfide gas is recovered and the recovered waste hydrogen sulfide gas is supplied to the process plant through the pipe.

    Abstract translation: 本发明的目的是提供一种能够回收排出的废硫化氢气体并有效地将气体供给到通过使用硫化氢气体进行加工的工艺设备的硫化氢气体生产设备,并且还提供回收和使用废氢 硫化氢气体由硫化氢气体生产厂。 在本发明中,硫化氢气体生产装置设置有回收从硫化氢气体制造装置排出的废硫化氢气体的管道,其一端与使用硫化氢气体的处理装置连接, 回收排出的废硫化氢气体,回收的废硫化氢气体通过管道供给工艺装置。

    Flash vessel and method for operating same
    7.
    发明授权
    Flash vessel and method for operating same 有权
    闪存容器及操作方法

    公开(公告)号:US09464341B2

    公开(公告)日:2016-10-11

    申请号:US14370882

    申请日:2012-12-27

    Abstract: A hydrostatic tower whose lower part communicates with a liquid phase space within a flash vessel, and whose upper part communicates with a gas phase space within the flash vessel is provided. A rising liquid level within the hydrostatic tower is detected by at least one maximum liquid level sensor provided at a position at the same level as a predetermined maximum liquid level within the liquid phase space. A dropping liquid level within the hydrostatic tower is detected by at least one minimum liquid level sensor provided at a position at the same level as a predetermined minimum liquid level within the liquid phase space.

    Abstract translation: 提供了一种静水塔,其下部与闪光容器内的液相空间连通,并且其上部与闪蒸容器内的气相空间连通。 静液压塔内的上升液位由设置在与液相空间内的预定最大液面相同水平的位置处的至少一个最大液位传感器检测。 流体静力塔内的液滴液位由至少一个液位传感器检测,该液位传感器位于与液相空间内的预定最小液位相同的位置上。

    FLASH VESSEL AND METHOD FOR OPERATING SAME
    8.
    发明申请
    FLASH VESSEL AND METHOD FOR OPERATING SAME 有权
    闪光灯及其操作方法

    公开(公告)号:US20150145183A1

    公开(公告)日:2015-05-28

    申请号:US14370882

    申请日:2012-12-27

    Abstract: A hydrostatic tower whose lower part communicates with a liquid phase space within a flash vessel, and whose upper part communicates with a gas phase space within the flash vessel is provided. A rising liquid level within the hydrostatic tower is detected by at least one maximum liquid level sensor provided at a position at the same level as a predetermined maximum liquid level within the liquid phase space. A dropping liquid level within the hydrostatic tower is detected by at least one minimum liquid level sensor provided at a position at the same level as a predetermined minimum liquid level within the liquid phase space.

    Abstract translation: 提供了一种静水塔,其下部与闪光容器内的液相空间连通,并且其上部与闪蒸容器内的气相空间连通。 静液压塔内的上升液位由设置在与液相空间内的预定最大液面相同水平的位置处的至少一个最大液位传感器检测。 流体静力塔内的液滴液位由至少一个液位传感器检测,该液位传感器位于与液相空间内的预定最小液位相同的位置上。

    Operation method for dezincification plant

    公开(公告)号:US09751035B2

    公开(公告)日:2017-09-05

    申请号:US14760066

    申请日:2013-12-10

    CPC classification number: B01D37/04 C01G9/08 C22B1/00 C22B23/043 C22B23/0461

    Abstract: At the beginning of a dezincification plant used in a dezincification step in a hydrometallurgical method for nickel, a decrease throughout the dezincification plant is controlled to prevent a decrease in production volume and a cake layer is formed on a filter cloth provided to a filter device inside the dezincification plant. At the beginning of dezincification plant, a slurry containing a formed zinc sulfide is supplied to a filter for filtration and separation, an adjustment is performed in which the flow rate of the slurry is increased to reach a target flow rate in a time T2 which satisfies the following relational expression 3×T1≦T2≦5×T1, where T1 represents the time between starting a slurry supply and attaining the target flow rate in the case of transferring the slurry at the maximum liquid transfer capacity of a pump configured to transfer the slurry.

    AUTOCLAVE APPARATUS USED DURING HIGH-PRESSURE ACID LEACHING PROCESS
    10.
    发明申请
    AUTOCLAVE APPARATUS USED DURING HIGH-PRESSURE ACID LEACHING PROCESS 有权
    高压酸浸过程中使用的自动装置

    公开(公告)号:US20150152521A1

    公开(公告)日:2015-06-04

    申请号:US14406492

    申请日:2013-06-10

    Abstract: In an autoclave apparatus for a high-pressure acid leaching process which advances leaching by stirring heated and pressurized material slurry and sulfuric acid by stirrers in compartments in an autoclave main body of a plurality of compartments, transfers slurry from an upstream side compartment to a downstream one to advance leaching, liquid flow ports for slurry transfer that open and close by doors are provided on the partition walls, the liquid flow ports for slurry transfer are installed at positions where the heights from the lowermost portion the autoclave to the center of gravity are 0.1 to 0.3 times an autoclave diameter and distances from the center lines of the partition walls to the center of gravity are 0.05 to 0.25 times the autoclave diameter, and the liquid flow ports for slurry transfer have shapes which do not reach end portions of the partition walls.

    Abstract translation: 在用于高压酸浸法的高压釜装置中,其通过在多个室的高压釜主体中的隔室中搅拌加热和加压的材料浆料和硫酸搅拌器进行浸出,将浆料从上游侧隔室转移到下游 一个用于推进浸出的液体流通端口用于通过门打开和关闭的用于浆料转移的液体流动端口设置在分隔壁上,用于浆料转移的液体流动端口安装在从高压釜的最下部分到高度的高度位置 高压釜直径的0.1〜0.3倍,从隔壁的中心线到重心的距离为高压釜直径的0.05〜0.25倍,浆料输送用的液体流通孔的形状不会到达分隔部的端部 墙壁

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