Method of manufacturing multiple fuel cell separator plate assemblies

A method of manufacturing a flow field plate, comprising:

• mixing graphite and resin materials;
• feeding the graphite and resin materials into an extruder having a length including a first portion comprising ¼ of the length of the extruder, a second portion comprising ½ of the length of the extruder, and a third portion comprising ¼ of the length of the extruder;
• heating the graphite and resin materials to provide a molten graphite and resin mixture in the extruder, the heating including providing an increasing temperature profile from 150 degrees Celsius to 350 degrees Celsius along the first portion, maintaining a flow field temperature of 350 degree Celsius along the second portion, and providing a decreasing temperature profile from 350 degrees Celsius to 250 degrees Celsius along the third portion;
• forming the molten graphite and resin mixture into a continuous flow field plate, the forming including extruding the molten graphite and resin mixture through a die, wherein the extruding includes forming flow field channels in the continuous flow field plate with channels and ribs of the die, the die located at an exit of the extruder and having a die length, the die length being ⅓ of the length of the extruder and including the third portion and part of the second portion to provide a decreasing temperature profile along a portion of the die from 350 degrees Celsius to 250 degrees Celsius, wherein during the forming, the resin material has a liquid to solid phase ratio between 40:60 and 60:40 at an exit of the die;
• and
• separating the continuous flow field plate into discrete flow field plates.

A method of manufacturing a flow field plate, comprising:

• mixing flake graphite and fluorinated ethylene propylene resin materials;
• feeding the flake graphite and fluorinated ethylene propylene resin materials into an extruder having a length including a first portion comprising ¼ of the length of the extruder, a second portion comprising ½ of the length of the extruder, and a third portion comprising ¼ of the length of the extruder, the feeding including providing a discontinuous material feed to the extruder;
• cooling the flake graphite and fluorinated ethylene propylene resin materials proximate an entrance of a barrel of the extruder;
• heating the flake graphite and fluorinated ethylene propylene resin materials to provide a molten graphite and resin mixture in the barrel of the extruder, the heating including providing an increasing temperature profile along the first portion, maintaining a temperature along the second portion that is a melting point of the fluorinated ethylene propylene resin, and providing a decreasing temperature profile along the third portion;
• forming the molten graphite and resin mixture into a continuous flow field plate from the discontinuous material feed, the forming including extruding the molten graphite and resin mixture through a die at an exit of the extruder, the die having a die length that is ⅓ of the length of the extruder such that the die has the maintained temperature along a first region and the decreasing temperature profile along a second region, the forming further including forming flow field channels in the continuous flow field plate during the extruding via ribs and channels of the die, wherein the extruding further includes depositing the flake graphite and fluorinated ethylene propylene resin materials into the barrel of the extruder and slidably translating a ram through the barrel without rotating the ram about an axis of the ram to force the molten graphite and resin mixture through the die and, wherein during the forming, the resin material has a liquid to solid phase ratio between 40:60 and 60:40 at an exit of the die;
• and
• separating the continuous flow field plate into discrete flow field plates.