Raw Ore: Sulfide-Type Molybdenum Ore (Molybdenite) Head Grade: 0.15% Mo Concentrate Grade: ≥ 55% Mo
We can provide different type graphitization furnace for changing carbon material into graphite include lengthwise graphitization furnace (LWG furnace), Acheson graphitization furnace (AC furnace) and Box type graphitization furnace (Box Furnace). Graphitization processing has different heating curve and treatment cycle for anode material, special graphite, Isostatic graphite, HP electrode & pins, UHP electrodes & pins.
Design temperature: Max. 3100°C
Loading capacity: 220t per furnace
HP electrode, UHP electrode baking and rebaking process; Artificial graphite anode material precarbonization process; Special graphite and Isostatic graphite…
The disordered microcrystalline structure formed by a large number of carbon atoms is ordered, the interlayer spacing is reduced, thereby obtaining the physical and chemical properties required for artificial graphite anode materials.
The carbonaceous material in the crucible is subjected to high temperature heat treatment to make it have the characteristics of graphite crystal structure.
Apart from the Acheson furnace, Prominer can also design the length-wise graphitization furnace and grid box graphitization furnace. Formaking the high end anode materials, the Acheson furnace is more stable and mature.
LWG furnaces are more efficient in UHP Graphitization, the working time is reduced from 80 hours/furnace to 24 hours/furnace with lower power consumption.
The box-type graphitization is based on the Acheson graphitization furnace, and a carbon plate box is set in the furnace, which is equivalent to the enlargement of the crucible ruler, thereby bringing a higher single-furnace output.
Graphitization accounts for about 50% of the cost of artificial graphite and is an important processing link of artificial graphite.
The LWG process heats the product directly for electrode processing, but need crucible for Anode material.
Our equipment with the main Technical Parameters as below
| Feature | LWG Furnace | Acheson Furnace | Box Furnace: |
|---|---|---|---|
| Design temperature: | Max. 3000°C | Max. 3100°C | Max. 3050°C |
| Crucible or Saggar | Need crucible for Anode material, no need for electrode | Need crucible for Anode material, no need for electrode | No need |
| Packing Material: | Need | Need | Need |
| Application: | UHP electrode, Isostatic graphite special graphite, anode material | UHP electrode, Isostatic graphite special graphite and anode material | Specially designed for anode materials |
| The details below base on processing the Anode material for lithium battery | |||
| Power consumption: | 9000-12000 kWh/t | 11000-15000 kWh/t | 7500-12000 kWh/t |
| Yield rate | Not less than 94% | Not less than 96% | Not less than 90% |
| Graphitization degree | around 93% | around 95% | around 94% |
| Loading Capacity: | Max. 30 ton per furnace | Max. 80 Tons per furnace | Max. 220 Tons per furnace |
| Design temperature | Max. 2900°C |
| Loading way | Need crucible for anode material, no need for electrode |
| Packing material | Need CPC coke as thermal insulating material |
| Application | UHP electrode, Isostatic graphite special graphite and Anode material |
| The details below base on processing the Anode material for lithium battery | |
| Power consumption | 9000-12000 kWh/t |
| Yield rate | Not less than 94% |
| Graphitization degree | around 93% |
| Loading Capacity | Max. 30 ton per furnace |
| Design temperature | Max. 3100°C |
| Loading way | Need crucible for anode material, no need for electrode |
| Packing material | Need CPC coke as thermal insulating material |
| Application | UHP electrode, Isostatic graphite special graphite, Anode material |
| The details below base on processing the Anode material for lithium battery | |
| Power consumption | 11000-15000 kWh/t |
| Yield rate | Not less than 96% |
| Graphitization degree | around 95% |
| Loading Capacity | Max. 80 ton per furnace |
| Design temperature | Max. 3050°C |
| Loading way | No need crucible for anode material |
| Packing material | Need CPC coke as thermal insulating material |
| Application | Special graphite and Anode material |
| The details below base on processing the Anode material for lithium battery | |
| Power consumption | 7500-12000 kWh/t |
| Yield rate | Not less than 90% |
| Graphitization degree | around 94% |
| Loading Capacity | Max. 220 ton per furnace |
Prominer can provide the service work as below
Raw Ore: Sulfide-Type Molybdenum Ore (Molybdenite) Head Grade: 0.15% Mo Concentrate Grade: ≥ 55% Mo
Raw Material: Existing gold plant tailings (All-slime) Gold Grade in Tailings: 1.2 g/t Final Product: Gold Ingot
Raw Ore: Sulfide Type Copper Ore (Mainly Chalcopyrite) Copper Grade: 0.8% Final Product: Copper Concentrate
Raw Material: Gold mine tailings slurry from CIL plant Tailings Solids Content: 35-40% Final Stacking Density: 1.6-1.8 t/m³
Raw Material: Spent gold leaching solution (cyanide-based) Gold Concentration in Solution 2-5 ppm
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3000 TPD Gold Flotation Project in Shandong Province
2500TPD Lithium Ore Flotation in Sichuan
Fax: (+86) 021-60870195
Address: No.2555,Xiupu Road, Pudong, Shanghai
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