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74                                                              Tackifiers





























            Figure 6.1. Commercial pulping processes. [Adapted, by permission, from Höfer, R, The Pine Biorefinery
            Platform Chemicals Value Chain, Industrial Biorefineries and White Biotechnology, Elsevier, 2015,
            pp. 127-55.]

                Several  families  of  resins  and  their  derivatives  are  typically  used  as  tackifiers,
            including
                •  hydrocarbon resins (petroleum-based feedstocks)
                •  hydrogenated hydrocarbon resins (petroleum-based feedstocks)
                •  aromatic polymers and copolymers (petroleum-based feedstocks)
                •  glycerol esters of rosin (wood, gum (sap), and paper-making (tall oil) rosin)
                •  rosin  (wood,  gum  (sap),  and  paper-making  (tall  oil)  rosin)  and esters of pen-
                   taerythritol
                •  polyterpenes (derived from wood or citrus fruits)
                Typical properties of these groups of tackifiers are given in the separate tables below.
                The above tackifiers are available in the forms of solids, molten solids, and water
            dispersions.
                Applications  of  tackifiers  are  widespread  including  assembly  adhesives,  asphalt
            modification, automotive, bookbinding, building and construction, caulks, coatings, floor-
            ing, footwear, graphic arts, hot-melt adhesives, hygiene, labels, leather, lithographic inks,
            nonwovens, packaging, paints, pressure-sensitive adhesives, printing inks, rubber com-
            pounding, sealants, tapes, varnish, wire and cable, and woodworking.
            6.1 METHODS AND MECHANISMS OF TACK ENHANCEMENT

                                                                               1
            Figure 6.1 shows the outcomes of the commercial alkaline kraft pulping process.  The
            crude tall oil consists of approximately 35-50% fatty acids, 15-55% rosin acids, and 5-
            35% unsaponifiable and neutral material. It can be separated into its components (bottom
                                                                           1
            of Figure 6.1) by vacuum and steam-assisted fractional distillation procedures.  The acids
            can be further processed by esterification, which, depending on the alcohol used, lead to
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