Page 395 - Materials Chemistry, Second Edition
P. 395

Appendix A Solution of Exercises  379

               Solution of exercise: Allocation per mass in a process chain (anonymised case
               example) (Section 3.3.2.2)

               Starting point for the consideration of allocation is the 33 t end product.
               • Production end product: no allocation; 154 GJ are fully assigned to the 33 t end
                product.
               • Production intermediate product: allocation according to mass:
                  3106 GJ are assigned to 247 t co-product (88.2%) and
                  415 GJ are assigned to 33 t intermediate product (11.8%).
                  If no loads would be attributed to the co-product, it would not carry any loads
                   of the process.
               • Steam cracker: One product of the steam cracker is 280 t ethene (37.2% of
                products), that is processed in the plant ‘production of intermediate product’.
                Of the loads that are allocated by mass in the steam cracker to the 280 t ethene
                (2590 GJ) only 11.8% (306 GJ) are to be assigned to the intermediate product. The
                remaining 88.2% have to be assigned to the co-product. Otherwise the co-product
                would not carry any load of the pre-production.
               • Atmospheric distillation: One product of the atmospheric distillation is 935 t
                Naphtha (14.7%) that is processed in the steam cracker. Of the loads that are
                allocated by mass in the atmospheric distillation to the Naphtha (484 GJ) only
                37.2% (180 GJ) are to be assigned to the Ethene. Otherwise the other products of
                the steam cracker would carry no loads of the atmospheric distillation. Of this
                180 GJ only 11.8% (21 GJ) are to be assigned to the intermediate product. The
                remaining 159 GJ have to be assigned to the co-product.
               • Consequently the loads for the production of 33 t end product sum up as follows:


                             Process                         GJ

                             Production end product         154
                             Production intermediate product  415
                             Steam cracker                  306
                             Atmospheric distillation        21
                             Sum                            896


                This corresponds to 27 MJ kg −1  end product.



               Solution of exercise: Closed-loop recycling of production scraps (Section 3.3.3)

               1.  Calculation of raw material and energy consumption without recycling:
                  In this case the scrap is treated as waste and therefore no load is allocated.
   390   391   392   393   394   395   396   397   398   399   400