Page 177 - Small Animal Clinical Nutrition 5th Edition
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Commercial Pet Foods        179



                  Compounding and Mixing
        VetBooks.ir  Good compounding (physically combining all of the dry mix
                  ingredients) and mixing are essential to delivering a consistent,
                  nutritionally adequate product. Improper compounding will
                  result in unequal distribution of essential nutrients or lack of
                  key ingredients in a product.
                    Ground bulk ingredients are usually stored in large bins.
                  From here, they are blown, via negative airflow, into mixing
                  hoppers. Ingredients that form a smaller percentage of the
                  product can be added by hand and combined with bulk ingre-
                  dients. Computer-controlled scales weigh dry mix ingredients
                  to ensure they are present in desired quantities.
                    After a “batch” of dry mix is compounded it must be proper-
                  ly mixed. Mixer types and times are carefully selected based on
                  the flow characteristics of the ingredients that compose the
                  mixture. Because particle size, density and shape influence flow
                  characteristics, a ribbon blender is often used for thorough mix-
                                                                      Figure 8-14. Extruder preconditioner used in commercial pet food
                  ing (Harnby, 1993). A ribbon blender is a horizontal blending  production. The mixing and conveying paddles shown here initiate
                  machine that has a shaft running through the middle of the  starch gelatinization and move the dry mix toward the extruder for
                  mixer. A ribbon of steel attached to the shaft is the mixing ele-  cooking.
                  ment. A ribbon blender is able to thoroughly mix large quanti-
                  ties of dry ingredients (up to 5,000 kg) and is the most com-  through a multi-holed die where it is cut to the desired length
                  monly used mixing device. After the finished dry mix is ground  by a rotating knife (Figures 8-15 through 8-17). This type of
                  for the last time, it is transferred to the extrusion process area  extruder operates on the principle of friction.The desired cook-
                  and stored in a bin.                                ing of the dough is achieved when the material comes in con-
                                                                      tact with the barrel wall (Johnson, 1993). The most common
                  Extrusion                                           type of single-screw extruder used in the pet food industry is
                  Extrusion is the primary processing method for commercial-  called a high shear cooker extruder (Dziezak, 1989).
                  ly prepared dry and semi-moist pet foods. The process itself  The process conditions of the single-screw extruder can be
                  can be thought of in terms of bread making: mixing, knead-  adjusted to produce different types of products. For example,
                  ing, proofing (rising of the dough), shaping, rising and slic-  a high-fiber, low-fat formula produces significantly more fric-
                  ing (Figure 8-13).The first step in extrusion cooking is prop-  tion, and is therefore more prone to overcooking than more
                  er preconditioning of the dry mix to start gelatinization of  conventional formulas. Reducing the screw speed, screw pro-
                  the starches.                                       file, feed rate or amount of preconditioning, increasing the fat,
                    The dry mix is fed into the preconditioner by a weighing sys-  which helps lubricate the extruder barrel or a combination of
                  tem that accurately maintains a constant feed rate.The precon-  these factors will compensate for this processing challenge by
                  ditioner contains mixing/conveying paddles (Figure 8-14) that  reducing the cook time (residence time). Residence times can
                  mix the dry mix and liquid additions (fat, meat slurries, etc.),  be varied from 10 to 270 seconds with temperatures ranging
                                                                                  º
                  along with water and steam to increase the moisture content  from 80 to 200 C (Dziezak, 1989). Because of the ingredient
                  and prepare the mixture for cooking and forming. Generally,  matrix used in pet foods, a high-temperature, short residence
                  the dry mix and any liquid additions are retained in the precon-  time (HTST) approach is used.The benefits of HTST extru-
                  ditioner for about 45 seconds.The preconditioner achieves a 20  sion include: 1) complete cooking, 2) destruction of microor-
                  to 25% cook of the starch (a measure of the completeness of  ganisms and 3) denaturing of anti-nutritional factors such as
                  extrusion cooking). Extrusion provides much more flexibility in  trypsin inhibitor and hydrolytic enzymes that lead to rancid-
                  processing different formulations than do pelleting or baking  ity (Dziezak, 1989). Nutrient losses, however, are also
                  technologies (Box 8-7).                             incurred because of the high temperatures and shear forces
                                                                      (Box 8-8). Vitamin A and E losses of 21 to 26% and thiamin
                    SINGLE-SCREW EXTRUDERS                            losses of 12% may occur (Frye, 1995). Adding higher levels of
                    Single-screw extruders were originally used in the plastics  these vitamins compensates for losses during extrusion.
                  industry and later converted to all types of food applications
                  and are used by approximately 90% of pet food manufacturers  TWIN-SCREW EXTRUDERS
                  (Rokey, 1995). Extruders come in a variety of sizes from pilot  Similar to the single-screw extruder, the twin-screw extruder
                  plant prototype machines to large volume machines capable of  was borrowed from the plastics industry and introduced to the
                  extruding 12 to 15 tons of food per hour. Single-screw extrud-  food industry in the early 1970s (Dziezak,1989).As their name
                  ers consist of a cylindrical multi-segmented barrel with a single  implies, twin-screw extruders have components similar to those
                  screw that propels, mixes and cooks the material and forces it  of single-screw extruders, except there are two screws. These
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