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               254                                                                                    Pulp and Paper


                                                   −
                                                           −
                 In Kraft pulping the active reagents are HS and HO .  3. Other Options
               The Na 2 S exists in equilibrium with H 2 O and serves not
                                                                 There are numerous alternatives that have been proposed
               only as a source of HS , but also as an additional source
                                 −
                                                                 and that are being implemented. These include the addi-
               of NaOH according to the following:
                                                                 tion of anthraquinone to soda and Kraft processes; the use
                         H 2 O + Na 2 S   NaHS + NaOH.    (1)    of ferric oxide in the soda pulping process (DARS pro-

                                                                 cess) and the substitution of sodium metaborate (NaBO 2 )
               The actual mechanisms of Kraft delignification are highly  for NaOH in Kraft pulping (borate based autocausticiz-
               complex, revolving around the ionization of acid phenolic  ing). These options largely are designed to achieve pro-
                                −
               units in lignin by OH and nucleophilic displacement of  cess advantages. Anthraquinone (AQ) addition improves
               lignin units with HS . The chemistry of delignification is  pulping yield by 1–3%. Its utility, however, is limited to
                               −
               reviewed in detail elsewhere. It is sufficient to note here the  alkaline systems and its economics are dependent upon the
               conditions specified above and the pulp yields; typically  trade-off between raw material and chemical costs. DARS
               45–55% of the dry weight of wood furnish is produced as  and borate-based Kraft pulping are designed to simplify
               Kraft pulp.                                       chemical recovery. The DARS process is applicable only
                                                                 to sulfur-free systems.
                                                                   Other options include oxygen pulping as well as oxy-
                 2. Sulfite and Soda Pulping
                                                                 gen bleaching, discussed later in the chapter. A consid-
               It is useful to compare Kraft pulping to sulfite pulp-  erable amount of research has been expended on totally
               ing as a means for understanding differences among  new approaches to pulping wood and agro-based mate-
               these systems. Such a comparison is shown in Table III.  rials and include sulfur free organosolv (organic solvent)
               Conditions and results for soda pulping are also shown  pulping and biopulping. Organosolv pulping typically em-
               in  Table  III.  Kraft  pulping  is  presented  to  facilitate  ploys aqueous organic solvents such as ethanol, methanol
               comparison.                                       or acetic acid as the pulping liquor. Pollution problems
                 From Table  III, the similarities and differences among  are considerably reduced with these methods because the
               processes become apparent. Certainly the domination of  solvents have to be completely recovered for economic
               sodium as a base, and sulfur as an active reagent, become  reasons; and consequently, this also results in recovery
               obvious. The narrow range of cooking temperatures and  and usage of all the formerly discarded wood compo-
               yields also becomes apparent. What is not shown is the  nents. Another advantage is the potential for developing
               strength advantage of Kraft pulp. Also not shown are such  small, competitive pulp mills with lower capital invest-
               process considerations as chemical and energy recovery.  ment. Two organosolv pulp mills, one each based on 50%


                     TABLE III Pulping Conditions and Results for Sulfite and Soda Pulping a

                                             pH        “Base”         Active    Max temp  Time at max  Yield
                                                                                  ◦
                          Pulping method    range     alternatives    reagents    ( C)   temp (min)  (percent)
                                                            +
                     Acid bisulfite           1–2  Ca 2+ ,Mg 2+ ,Na ,NH +  HSO 3 −H +  125–145  180–420  45–55
                                                                 4
                     Bisulfite                3–5  Mg 2+ ,Na ,NH +    HSO ,H +   150–170   60–180    50–65
                                                                        −
                                                        +
                                                            4           3
                     Two-stage sulfite (Stora type)                                                  50–60
                                                                        −
                       Stage 1               6–8        Na +         HSO ,SO 2−  135–145  120–360
                                                                        3   3
                       Stage 2               1–2        Na +         HSO 3 ,H +  125–140  120–240
                     Three-stage sulfite (Silvola type)                                              34–45
                                                                        −
                       Stage 1               6–8        Na +         HSO ,SO 2−  120–140  120–180
                                                                        3
                                                                            3
                       Stage 2               1–2        Na +         HSO 3 ,H +  135–145  180–300
                       Stage 3               6–10       Na +         HO −       160–180   120–180
                     NSSC                    5–7      Na ,NH + 4     HSO ,SO 2−  160–180  15–180   75–90 b
                                                        +
                                                                        −
                                                                        3
                     Alkaline sulfite         9–13       Na +         SO 2− ,HO −  160–180  180–300  45–60
                                                                       3
                     Soda                   13–14       Na +         HO −       155–175   120–300  50–70 b
                     (Kraft)                13–14       Na +         HO ,HS −   155–175    60–18    45–55
                                                                       −
                       a From Sjostrom (1981). “Wood Chemistry: Fundamentals and Applications,” Academic Press, New York.
                       b Hardwood.
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