Background technology
The system fluorine carbon anode is a kind of advanced carbon material that is made of decolorizing carbon, has high strength, low degree of graphitization, low resistivity, anticorrosive, and characteristics such as especially anti-fluorine gas corrosion are the critical materials of industrial electrolysis system fluorine.Fluorine gas is mainly used in nuclear industry, is the main industrial chemicals of producing nuclear fuel.Along with nuclear industry development to the increasing rapidly of fluorine gas demand, require the system fluorine carbon anode to possess higher system fluorine efficient (anodic current density and steadily the cycle of operation).
The principal element that restriction carbon anode system fluorine efficient improves is the polarization of carbon anode.So-called polarization is meant: during electrolysis system fluorine, fluorine gas that produces in the electrolyzer and the reaction of the greying constituent element in the carbon anode are at the rete of anode surface generation based on covalent type fluorographite (CFX).This fluorographite hinders electron migration, significantly reduces the wettability of KF-2HF electrolytic solution antianode, is the compound of a kind of insulation or poor electric conductivity.Its existence will sharply reduce electrolytic efficiency, make system fluorine process hard to carry on.Meanwhile, follow the swelling that polarizes and come, will cause the local disengaging of carbon anode plate, fracture.
The anti-Polarization technique of system fluorine carbon anode of current main employing is the non-graphitized technology of carbon anode matrix.Promptly pass through the non-graphitized of each constituent element of carbon anode, delay polarization process, improve the carbon anode life-span.But because carbon is a kind of heterogeneous body mixture, can unavoidably sneak into the greying constituent element in the Industrial processes, the effect of this method is often not good enough; And because the conductivity of carbon material reduces with degree of graphitization, the non-graphitized conductivity that also will reduce carbon anode of matrix influences anodic current density and improves.
Summary of the invention
In order to solve the polarization problem of system fluorine carbon anode, the invention provides the difficult polarization of a kind of system fluorine carbon anode chemical vapor deposition pyrocarbon coating preparation method, improve the anti-polarization performance of carbon anode.
System fluorine carbon anode chemical vapor deposition pyrolytic carbon polarization resistant coating production comprises the steps:
Adopt ultrasonic cleaning carbon anode surface blot; Press gas volume per-cent: C
3H
635%~65%, N
265%~35% preparation carbon source gas; Carbon anode is placed chemical vapor deposition stove, and at 800~1200 ℃ of furnace temperature, furnace pressure 0.5~5KPa deposit 1~20h, the control furnace gas flows to, and obtains and tight, the uniform pyrocarbon coating of thickness of matrix bond; By concentration 1.5mol/l preparation nickel nitrate aqueous solution,, carbon anode is placed above-mentioned electroplate liquid, with current density 0.6mA/cm as electroplate liquid
2Electroplate 5~15min; Ultrasonic cleaning carbon anode surface blot, oven dry; 1040 ℃,<the 10Pa vacuum under thermal treatment 8~16h, obtain the pyrolytic carbon polarization resistant coating that pyrocarbon coating and metal particle mix and combine.
Adopt the present invention, gained chemical vapor deposition pyrolytic carbon coat-thickness is even, tight with the carbon anode matrix bond; With low greying, difficult polar chemical vapor deposition pyrolytic carbon sealing carbon anode surface pore, stop electrolytic solution to infiltrate the guard electrode internal structure to electrode interior; Form surface metal particle doped layer, formation conductive ion type or half ionic graphite intercalation compound layer when helping electrolysis system fluorine (CX ' F), stop the generation of non-conductive fluorographite, improve the surface conduction performance, anodic current density is greater than 0.1mA/cm
2, effectively prevent the polarization of carbon anode plate; The chemical vapor deposition pyrolytic carbon coating is mixed with the metal particle and is combined, and improves the anti-polarization performance of carbon anode jointly.
Embodiment
Provide following examples in conjunction with content of the present invention:
EXAMPLE l
At first, ultrasonic cleaning carbon anode surface blot, oven dry.Secondly, press gas volume per-cent: C
3H
635%, N
265% preparation carbon source gas.Carbon anode is placed chemical vapor deposition stove, and 800 ℃ of furnace temperature of control, furnace pressure 5Kpa and furnace gas flow to, deposition 20h.Once more, by concentration 1.5mol/l preparation nickel nitrate aqueous solution, carbon anode is placed electroplate liquid, with current density 0.6mA/cm
2Electroplate 5min.Ultrasonic cleaning carbon anode surface blot and oven dry.At last, 1040 ℃,<the 10Pa vacuum under thermal treatment 8h.
Embodiment 2
At first, ultrasonic cleaning carbon anode surface blot, oven dry.Secondly, press gas volume per-cent: C
3H
635%, N
265% preparation carbon source gas.Carbon anode is placed chemical vapor deposition stove, and 1000 ℃ of furnace temperature of control, furnace pressure 3Kpa and furnace gas flow to, deposition 10h.Once more, by concentration 1.5mol/l preparation nickel nitrate aqueous solution, carbon anode is placed electroplate liquid, with current density 0.6mA/cm
2Electroplate 10min.Ultrasonic cleaning carbon anode surface blot and oven dry.At last, 1040 ℃,<the 10Pa vacuum under thermal treatment 12h.
Embodiment 3
At first, ultrasonic cleaning carbon anode surface blot, oven dry.Secondly, press gas volume per-cent: C
3H
635%, N
265% preparation carbon source gas.Carbon anode is placed chemical vapor deposition stove, and 1200 ℃ of furnace temperature of control, furnace pressure 1Kpa and furnace gas flow to, deposition 1h.Once more, by concentration 1.5mol/l preparation nickel nitrate aqueous solution, carbon anode is placed electroplate liquid, with current density 0.6mA/cm
2Electroplate 15min.Ultrasonic cleaning carbon anode surface blot and oven dry.At last, 1040 ℃,<the l0Pa vacuum under thermal treatment 16h.
Embodiment 4
At first, ultrasonic cleaning carbon anode surface blot, oven dry.Secondly, press gas volume per-cent: C
3H
650%, N
250% preparation carbon source gas.Carbon anode is placed chemical vapor deposition stove, and 900 ℃ of furnace temperature of control, furnace pressure 3Kpa and furnace gas flow to, deposition 5h.Once more, by concentration 1.5mol/l preparation nickel nitrate aqueous solution, carbon anode is placed electroplate liquid, with current density 0.6mA/cm
2Electroplate 8min.Ultrasonic cleaning carbon anode surface blot and oven dry.At last, 1040 ℃,<the 10Pa vacuum under thermal treatment 9h.
Embodiment 5
At first, ultrasonic cleaning carbon anode surface blot, oven dry.Secondly, press gas volume per-cent: C
3H
650%, N
250% preparation carbon source gas.Carbon anode is placed chemical vapor deposition stove, and 1100 ℃ of furnace temperature of control, furnace pressure 2Kpa and furnace gas flow to, deposition 3h.Once more, by concentration 1.5mol/l preparation nickel nitrate aqueous solution, carbon anode is placed electroplate liquid, with current density 0.6mA/cm
2Electroplate 12min.Ultrasonic cleaning carbon anode surface blot and oven dry.At last, 1040 ℃,<the 10Pa vacuum under thermal treatment 13h.
Embodiment 6
At first, ultrasonic cleaning carbon anode surface blot, oven dry.Secondly, press gas volume per-cent: C
3H
665%, N
235% preparation carbon source gas.Carbon anode is placed chemical vapor deposition stove, and 800 ℃ of furnace temperature of control, furnace pressure 4Kpa and furnace gas flow to, deposition 12h.Once more, by concentration 1.5mol/l preparation nickel nitrate aqueous solution, carbon anode is placed electroplate liquid, with current density 0.6mA/cm
2Electroplate 5min.Ultrasonic cleaning carbon anode surface blot and oven dry.At last, 1040 ℃,<the 10Pa vacuum under thermal treatment 9h.
Embodiment 7
At first, ultrasonic cleaning carbon anode surface blot, oven dry.Secondly, press gas volume per-cent: C
3H
665%, N
235% preparation carbon source gas.Carbon anode is placed chemical vapor deposition stove, and 900 ℃ of furnace temperature of control, furnace pressure 2Kpa and furnace gas flow to, deposition 8h.Once more, by concentration 1.5mol/l preparation nickel nitrate aqueous solution, carbon anode is placed electroplate liquid, with current density 0.6mA/cm
2Electroplate 10min.Ultrasonic cleaning carbon anode surface blot and oven dry.At last, 1040 ℃,<the 10Pa vacuum under thermal treatment 12h.
Embodiment 8
At first, ultrasonic cleaning carbon anode surface blot, oven dry.Secondly, press gas volume per-cent: C
3H
665%, N
235% preparation carbon source gas.Carbon anode is placed chemical vapor deposition stove, and 1000 ℃ of furnace temperature of control, furnace pressure 1Kpa and furnace gas flow to, deposition 5h.Once more, by concentration 1.5mol/l preparation nickel nitrate aqueous solution, carbon anode is placed electroplate liquid, with current density 0.6mA/cm
2Electroplate 15min.Ultrasonic cleaning carbon anode surface blot and oven dry.At last, 1040 ℃,<the 10Pa vacuum under thermal treatment 16h.