while the invention has broader utility , the following description will detail one preferred form wherein a ready - to - eat cereal product is treated with antioxidant to achieve processing efficiencies and improved product quality . as used herein , the term “ cereal product ” is meant to include completely processed ready - to - eat cereals as well as intermediate products , i . e ., half products . prominent among the cereals that can be treated by the process and apparatus of the invention are the various puffed , flaked , shredded and otherwise shaped and cooked forms of corn , rice , wheat , oats and the like . other products containing these and other cereals , as that term is known to those skilled in the art , can be treated . the usual cereal ingredients can be supplemented with dried fruits , edible nuts and milk or other proteinaceous ingredients . for example , dried fruit such as coconut , raisins and apricots may be employed . edible nuts such as almonds , walnuts and others may be used . the cereals can be mixed with these other products before or after treatment according to the invention . referring now to fig1 there is illustrated , in elevation , a view showing an application device of the invention 10 positioned in a conduit 12 between an elevated source of particulate material ( surge vessel 14 ) and a lower collection vessel ( wheeled tote 16 ). this arrangement permits the particulate material to be treated as it flows by gravity . the application device 10 shown in fig1 is illustrated in greater detail in fig2 and 3 , as having attachment flanges 13 and 13 a for incorporation into a larger conduit 12 . fig3 is a top plan view of a conduit containing a novel ingredient application device according to the invention , looking in the direction of flow of a particulate material to which the ingredient will be applied . fig2 is a cross sectional view taken along line 2 - 2 in fig3 . the apparatus is preferably constructed in main part of stainless steel , but can include nonstick surfaces where desired and practical . in operation , a particulate cereal material is fed through the passage in conduit 12 from an inlet 15 at the top to an outlet 17 at the bottom . the material is fed past a baffle 18 , which is suspended within the passage . because of its position and shape , the baffle deflects flow of particulate cereal material from the central zone of the passage toward the conduit wall , the area near the wall defining an application zone . the application zone is generally shown as the area 28 between the dashed lines and the wall of conduit 12 . while spread out within this application zone , one or more desired minor ingredients are applied to the particulate cereal material in the application zone . the minor ingredients can be antioxidants , colors , vitamin and / or mineral mixes , or the like . among the suitable antioxidants are bha ( 2 and 3 - tert - butyl - 4 - hydroxy - anisole ), tbhq ( tertiary butyl hydroquinone ), bht ( 3 , 5 - di - tert - butyl - 4 - hydroxytoluene ), propyl gallate and citric acid , which are typically added in small effective amounts up to a total of about , 0 . 002 %, e . g , about 20 p . p . m . ( weight to weight ). because the fda permits only 0 . 02 % ( 200 ppm ) total antioxidants ( based on fat weight ), carriers are typically used in solution formulations , including vegetable oil , propylene glycol , and / or mono - and diglycerides . among the suitable fat or oil carriers are safflower oil , sunflower oil , high oleic sunflower , corn oil , rice bran , soybean oil , sesame , peanut , olive , babassu nut , palm , cottonseed , low erucic rapeseed , and the like oils , with the more highly unsaturated oils being particularly preferred . typically , a manufacturer can recommend suitable solutions and application rates . any of a variety of spray means can be employed , including those designed for low pressure or high pressure , with or without the addition of a carrier fluid in one or more phases . among the suitable low - pressure devices are those effective to spray liquids under pressure without the use of a carrier fluid . simple spray nozzles of the hydraulic type are illustrated and preferred . the preferred nozzles of this type will typically emit spray in a conical pattern at a median angle α of about 45 ° minimum up to 75 ° maximum , relative to a central axis . preferred nozzles will produce an average droplet size of from about 350 to about 900μ , mean diameter . the viscosity and / or composition of the solution or dispersion being sprayed , and / or the pressure and nozzle design can be varied to achieve the best spray for the cereal product and applied ingredient concerned . [ 0031 ] fig2 and 3 illustrate a preferred arrangement including an airless spray means 20 positioned downstream of a conical baffle 22 to both distribute the cereal for effective spray application and to protect it from the downwardly moving stream of particulate cereal . the spray means 20 and baffle 22 are shown connected to a section of conduit 12 as will be further explained in connection with fig3 . the baffle 22 has an apex 24 pointed in the direction of the inlet 15 and an open base 26 facing the outlet 17 . the spray means 20 is positioned within the open base 26 of the conical baffle 22 ( and downstream of the apex 24 ) and directs a conical flow outward toward the application zone , generally the area 28 defined between the dashed lines and the wall of conduit 12 . the spray means 20 , in preferred forms will spray radially at an angle effective to direct a spray of ingredient onto the particulate cereal material while substantially all of said cereal material is present in said application zone . it will be noted that in the illustration , the conduit 12 has a central axis that is positioned substantially vertically and passes through the apex 24 and concentrically with a pattern defined by the spray of material from said spray means . the specific conical shape is found effective with puffed cereal products , but can be varied as the shape and density of the cereal product is varied . the descending cereal product is naturally tumbled as it passes beyond the area of spray in application zone 28 . reference to fig3 shows the interior of the conduit 12 illustrated in fig1 and 2 , looking in the direction of cereal flow . the conical baffle 22 is seen with apex 24 at the center . the conduit 12 can be seen with attachment flange 13 and spokes 30 , 30 ′ and 30 ″, e . g , of angled stainless steel , suspend the conical baffle 22 so that it is centered within the conduit . reference back to fig2 shows one arrangement for suspending the nozzle 20 within the open base of the conical baffle 22 , such as by means of support disc 34 . fluid supply conduit 36 supplies minor ingredient and sufficient carrier for the intended purpose . in addition to the spray nozzles described above , any of the available low - pressure liquid distribution means , such as a mechanical atomizer of the type employed to spray paints , a sonic atomizer , a simple valve extending to a tube with a dispersion device comprising a plurality of orifices to provide a fine spray , a pintle - controlled nozzle capable of adjustable spray patterns , or the like , can be employed . air - powered nozzles can also be utilized , but it is preferred to operate them with a minimum of air to reduce the cost of the equipment and the effect air may have on the product or spray pattern . in some circumstances air can be employed to advantage , for example maintaining the nozzle and / or baffle clean . among suitable high - pressure injectors are those similar in type to those employed for fuel injection , which can provide an effective means of easily controlling application rate or even stopping flow as desired . following application of the antioxidant or other minor ingredient , the product can be further processed to apply other coatings or to intermix it with other ingredients or it can be directly packaged , such as in sealed plastic bags with outer paperboard boxes . the following examples are provided to further illustrate and explain a preferred form of the invention and are not to be taken as limiting in any regard . unless otherwise indicated , all parts and percentages are by weight . this example presents one preferred embodiment of the invention wherein a puffed cereal product is fed from a surge hopper through a transport conduit , similar to that shown in fig1 to be collected within a product tote . the cereal product is defined generally as puffed oat and corn product having a bulk density of about 145 grams / liter and as passing through a number ¾ inch sieve ( 19 mm by 19 mm openings ). the cereal is allowed to pass by gravity through a conduit as 12 , having a diameter of 12 inches from an inlet , which is 8 feet above the apex 24 of conical baffle 22 . the baffle has a height of 8 inches and a diameter at its base of 6 inches . as cereal is fed by gravity down the conduit and past the baffle , it is spread out from the center and substantially against the wall of conduit 12 to form an application zone . a conical hydraulic spray nozzle having a spray tip recessed within the cone and spaced from the cone base by about 2 inches , sprays a solution of bht in corn oil at a rate of 300 liters per hour onto the descending cereal product , which is then naturally tumbled as it passes beyond the area of spray . the mean spray angle of the nozzle is about 60 ° and the average droplet size is about 700μ , mean diameter . this example presents another preferred embodiment of the invention wherein a puffed corn and wheat cereal product is treated with a vitamin mix . the cereal and apparatus are the same as use in example 1 , but the solution comprises vitamins b1 , b2 , b6 , b12 , niacinamide and folic acid in water , and the application rate is 107 liters per hour . the above description is intended to enable the person skilled in the art to practice the invention . it is not intended to detail all of the possible modifications and variations which will become apparent to the skilled worker upon reading the description . it is intended , however , that all such modifications and variations be included within the scope of the invention which is seen in the above description and otherwise defined by the following claims . the claims are meant to cover the indicated elements and steps in any arrangement or sequence which is effective to meet the objectives intended for the invention , unless the context specifically indicates the contrary .
ready - to - eat cereal is prepared in modified sequence utilizing an apparatus to efficiently apply antioxidant or other useful minor ingredients for ready - to - eat cereal products as they are being conveyed through a conduit , preferably by gravity . the apparatus includes a conduit having an inlet and an outlet , and an external wall defining a passage between the inlet and outlet . the passage has a central zone and a radially displaced application zone adjacent the external wall . a baffle is suspended within the passage to deflect a downward flow of particulate cereal material toward the application zone . a spray applies the minor ingredient onto the particulate cereal in the application zone . efficiencies in equipment and processing are achieved . storage life of cereal products awaiting further processing and , thus , final product quality , is enhanced .