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The present invention is directed towards a liquid storage apparatus for use in the sulfurization facility for sulfurizing a sulfate solution to produce a sulfide, the apparatus comprising a plurality of liquid storage vessels for storing a slurry or a filtrate after solid/liquid separation, a colle

The present invention is directed towards a liquid storage apparatus for use in the sulfurization facility for sulfurizing a sulfate solution to produce a sulfide, the apparatus comprising a plurality of liquid storage vessels for storing a slurry or a filtrate after solid/liquid separation, a collective conduit for collectively passing an inactive gas to be fed into the liquid storage vessels or an exhaust gas discharged from the liquid storage vessels, and a pressure control conduit for receiving the flow of the inactive gas and the exhaust gas in order to control the pressure at the inner side of the liquid storage vessels. The pressure control conduit is connected by a junction to the collective conduit and equipped with a pair of pressure control valves mounted at both, front and rear, sides of the junction communicating to the collective conduit.

대표청구항 ▼

1. A liquid storage apparatus for use as a sulfurization facility for sulfurizing a sulfate solution to produce a sulfide in the sulfurizing step of a wet smelting for nickel oxide ore, the apparatus comprising: a plurality of liquid storage vessels, wherein each vessel including a feed conduit for

1. A liquid storage apparatus for use as a sulfurization facility for sulfurizing a sulfate solution to produce a sulfide in the sulfurizing step of a wet smelting for nickel oxide ore, the apparatus comprising: a plurality of liquid storage vessels, wherein each vessel including a feed conduit for feeding a slurry after the sulfurizing after a sulfurizing reaction and a filtrate after a solid/liquid separation, a gas charge/discharge conduit for charging an inactive gas and discharging a gaseous component at gaseous phase as an exhaust gas, and a discharge conduit for discharging the slurry or the filtrate;a collective conduit arranged of a branched shape having a series of joints at one end of the collective conduit aligned in parallel with the gas charge/discharge conduits of respective said liquid storage vessels and connected via the joints to the gas charge/discharge conduits for collectively passing the inactive gas to be fed to the liquid storage vessels and the exhaust gas discharged from the liquid storage vessels; anda pressure control conduit for receiving at one end the inactive gas to be fed to the liquid storage vessels and releasing at an other end the exhaust gas discharged from the liquid storage vessels, wherein the pressure control conduit is connected by a junction to the one end of the collective conduit and is equipped with a pair of pressure control valves mounted on the collective conduit at both, front and rear, sides of the junction so that both the feed of the inactive gas to the liquid storage vessels and the discharge of the exhaust gas from the liquid storage vessels can be controlled by the pressure control valves. 2. The liquid storage apparatus of claim 1, wherein the pressure control conduit includes a pressure gage for measuring a pressure at an inner side of the liquid storage vessels. 3. The liquid storage apparatus of claim 1, wherein the inactive gas is a nitrogen gas. 4. A pressure control method for use with the liquid storage apparatus of claim 1, the method comprising: enabling of feeding the inactive gas with the one end of the pressure control conduit being connected to an inactive gas feed facility and of discharging the exhaust gas with the other end of the pressure control conduit being connected to a purifying facility for processing the exhaust gas;when the pressure at an inner side of the liquid storage vessels is lower than 0.5 kPa, feeding the inactive gas to the liquid storage vessels by adjusting the pressure control valve at an inactive gas feed facility side; andwhen a pressure at the inner side of the liquid storage vessels is higher than 1.0 kPa, discharging as the exhaust gas a gaseous component at gaseous phase in the liquid storage vessels by adjusting the pressure control valve at the purifying facility side. 5. The pressure control method of claim 4, wherein each of the liquid storage vessels receives the slurry or the filtrate from the feed conduit and discharges the slurry or the filtrate from the discharge conduit individually. 6. The liquid storage apparatus of claim 2, wherein the inactive gas is a nitrogen gas. 7. A pressure control method for use with the liquid storage apparatus of claim 2, the method comprising: enabling of feeding the inactive gas with the one end of the pressure control conduit being connected to an inactive gas feed facility and of discharging the exhaust gas with the other end of the pressure control conduit being connected to a purifying facility for processing the exhaust gas;when the pressure at an inner side of the liquid storage vessels is lower than 0.5 kPa, feeding the inactive gas to the liquid storage vessels by adjusting the pressure control valve at an inactive gas feed facility side; andwhen a pressure at the inner side of the liquid storage vessels is higher than 1.0 kPa, discharging as the exhaust gas a gaseous component at gaseous phase in the liquid storage vessels by adjusting the pressure control valve at the purifying facility side. 8. A pressure control method for use with the liquid storage apparatus of claim 3, the method comprising: enabling of feeding the inactive gas with the one end of the pressure control conduit being connected to an inactive gas feed facility and of discharging the exhaust gas with the other end of the pressure control conduit being connected to a purifying facility for processing the exhaust gas;when the pressure at an inner side of the liquid storage vessels is lower than 0.5 kPa, feeding the inactive gas to the liquid storage vessels by adjusting the pressure control valve at an inactive gas feed facility side; andwhen a pressure at the inner side of the liquid storage vessels is higher than 1.0 kPa, discharging as the exhaust gas a gaseous component at gaseous phase in the liquid storage vessels by adjusting the pressure control valve at a purifying facility side.