The process started with
paper made from cotton rags. Before the processing of wood pulp and chemical wood pulps in the mid-19th century, the dominant fibre source for paper making was cotton and linen rags. The cotton rag sheet produced for conversion to vulcanized fibre is made like a sheet suitable for saturating. A paper is made for saturating by omitting any sizing additive, either beater added or surface applied. Today most paper sheets made for writing, printing, and coating have internal (
beater added)
sizing provided by
rosin,
alkyl succinic anhydride (ASA), or
alkyl ketene dimer (AKD) and surface sizing provided by
starch. A sheet made for saturating would have none of those chemical ingredients. The unsized saturating cotton fibre paper prepared for vulcanized fibre would be passed through a vat containing a zinc chloride solution.
Zinc chloride Zinc chloride is highly soluble in water. The solution used in saturating the paper was 70
Baumé in density (1.93 specific gravity) and about . This is roughly a 70% percent zinc chloride solution. Zinc chloride is a mild
Lewis acid with a solution pH of about 4. Zinc chloride can dissolve cellulose, starch, and silk. The zinc chloride used in making vulcanized fibre swelled and
gelatinized the cellulose. The fibre swelling explains why paper filters cannot be used to filter zinc chloride solutions. It is also the reason why a number of paper plies were used to build up to the desired vulcanized fibre thickness, rather treating a single paperboard thickness. For instance, the practice was to use 8 paper plies of 0.04 mm thickness each, as opposed to a single paperboard ply of 0.32 mm.
Pressing Once the paper plies were saturated with the gelatinizing zinc chloride, they were pressed together. The pressing allowed intimate contact of the
cellulose fibres, thus promoting bonding between the cellulose chains. Once the bonding was established, the process of leaching out the zinc chloride from the vulcanized fibre could begin. The leaching (removal by diffusion out) of the zinc chloride was accomplished by subjecting the vulcanized fibre to successively less concentrated baths of zinc chloride. The rate at which this could occur was constrained by osmotic forces. If the rate at which the vulcanized fibre was subjected to lower and lower concentrations of zinc chloride solution were too rapid, the osmotic forces could result in ply separations. The final leaching bath concentration was 0.05% zinc chloride. Thicknesses up to 0.093” (=2.4 mm), can be made on continuous lines that stretch up to 1,000 feet (305m) in length.
Vats For thickness above 0.093” (2.4 mm) and up to 0.375” (9.5 mm), a discrete laminated sheet (similar in size (l x w) to plywood) was produced by the cutdown process. The cutdown sheets were racked and moved from vat to vat by overhead tracked cranes. Each vat was successively less concentrated until the desired 0.05% was reached. The thicker the material, the longer it took to leach the zinc chloride to 0.05%. For the thickest products, times of 18 months to 2 years were needed. The zinc chloride used in these processes was for the most part not consumed in achieving the desired bonding. Indeed any dilution of the zinc chloride resulting from the leaching was dealt with by using evaporators to bring the zinc chloride solution back to the 70 Baume needed for using it again for saturating. In a sense, zinc chloride can be thought of as a catalyst in the making of the vulcanized fibre.
Dried and pressed Once the vulcanized fibre is leached free of the zinc chloride, it is dried to 5 to 6 percent moisture, and pressed or
calendered to flatness. The continuous process-made vulcanized fibre could then be sheeted or wound up into rolls. The density of the finished vulcanized fibre is 2 to 3 times greater than the paper from which it starts. The density increase is the result of 10% machine direction shrinkage, 20% cross machine direction shrinkage, and 30% shrinkage in thickness. ==Properties==