Kraft Foods Holdings, Inc.

Kraft Foods Global Brands LLC

Intercontinental Great Brands LLC

Nabisco Technology Company

Apv Baker Inc.

Mihaelos N Mihalos

Theodore N Janulis

Jessica H Schwartzberg

Barbara E Baumann

Zena E Forte

Stephanie M Ferguson

Chris E Robinson

Domenico R Cassone

Lynn C Haynes

Joseph Fierro

Carol Wines

Louise Slade

Harry Levine

James M Manns

Diane Louise Gannon

Ning Zhou

Edward Douglas Howey

Sarwat Gabriel

Henry Fernandes

Jan Karwowski

Vani Vemulapalli

Alan John Kino

C Y (Eric) Wang

Jeanny E Zimeri

Kenchu Antonio Tham

Supapong Siris

Kenneth Maas

Srinivas Vangeepuram

Allison Antonini

Alexander Gong

C William Epperson

Rachel DeCagna

Lawrence Scher

Alex Gong

Jill Critchley

Jack Kitchell

Charles C Epperson

John Zabrodsky

Chris Wiggins

Peter Daines

Henry Clark

Laura A Gallagan

Theresa Volpe

Martin R Shute

Falguni Dharmendrakumar Chauhan

Maura E Collins Titone

Charles W Epperson

Priya Kalwani

Daniel H Levison

Meredith Ann Keiling

Timothy David Towers

Kenenth Maas

Janelle Marie Myers

Nimesh K Patel

Edward D Howey

Harry Ira Levine

Rachel Decagna

C Y Wang

A cheese slurry suitable for topical application on a snack product prior to baking includes natural cheese powder solids, an emulsifier, oil, water, and pregelatinized starch in amounts effective to provide a crispy topping having an appearance of melted cheese uniformly adhered to the outer surface of the baked dough product, and up to 1 percent reducing sugars, polyols, or a combination thereof and substantially no enzyme-modified cheese, buttermilk, whey, maltodextrins, or yeast extract so that the cheese slurry composition is resistant to undesirable browning and burning upon baking.

Cheese toppings for baked snacks suitable for prebake application

A foodstuff, and a method and system of making the same, comprises a biscuit having a generally planar top surface and a generally planar bottom surface. The biscuit includes first indicia on the top surface that has a plurality of projections that extend from the top surface. The biscuit also includes second indicia on the bottom surface that has an imprint recessed from the bottom surface.

Biscuit with debossing on top and bottom

A method for the production of a food item having a filling includes conveying a food item to a first filling station. The filling station has a first rotating stencil with a first plurality of filling discharge ports. At least one first filling segment is formed by discharging filling, through the discharge ports, onto the food item. The food item is conveyed to a second filling station. The second filling station has a second rotating stencil with a second plurality of filling discharge ports. At least one additional filling segment is formed by discharging filling, through the second plurality discharge ports, onto the food item wherein the at least one additional filling segment is disposed on the food item adjacent to the at least one first filling segment.

Process and system for depositing filling on a biscuit

Thin food cluster

A method for the continuous production of cookies having a high content of large inclusions, such as chocolate chips, nuts, and fruit pieces includes extruding a cookie dough containing the inclusions through a die orifice to obtain an extrudate dough rope, and cutting the extrudate dough rope with an ultrasonic cutting blade. The ultrasonic cutting severs the extrudate dough rope into dough pieces which fall onto a moving conveyer into a substantially uniform or regular array for uniform baking. The ultrasonic cutter is controlled to provide a roughened top surface on a dough piece to provide a home baked appearance upon baking, while cutting through the inclusions without substantial displacement of the inclusions which would cause pock marks on the surface of the dough piece, and without substantial dough piece weight variation.

Production of cookies having large particulates using ultrasonic wirecutting

A dough extruder is disclosed that is configured to provide a continuous dough rope suitable for cracker products using a straight extended low friction compression chamber and a die plate oriented substantially perpendicular to a laminar flow of the dough. In one embodiment, the extruder can have a compressive force sufficient to extrude a plastic mass in a laminar flow in the range of about less than 120 psi; a compression chamber providing for an interior coefficient of friction in the range of about 0.2 and 0.35; and a die plate horizontally aligned with the longitudinal axis of the compressive force.

Dough extruders and methods

Shredded whole grain products, such as ready-to-eat cereals, and sweet and savory snacks, such as whole grain shredded corn chips are continuously produced by pelletizing agglomerates of cooked, tempered, whole cereal grain particles. Cooked whole grains, such as corn and other non-gluten or low-gluten containing grains have a tendency to become hard and rubbery after cooking during the cooling and tempering process. The pelletization results in the production of whole grain pellets having a soft, pliable texture, which are shreddable into continuous net-like sheets on a mass production basis. The pelletizing may be at a pressure of about 200 psig to about 600 psig, preferably from about 400 psig to about 500 psig. The pelletizing temperature may be controlled to provide a pellet temperature of about 80&#xb0; F. to about 120&#xb0; F., preferably from about 90&#xb0; F. to about 110&#xb0; F., upon exiting the pelletizer.

Production of whole grain shredded products

A stabilized bran component and a stabilized whole grain flour containing the component are produced by subjecting a bran-enriched coarse fraction which contains bran, germ and starch to grinding or milling to reduce grittiness of the coarse fraction without substantially damaging the starch due to abrasion. The coarse fraction may be stabilized by heating to substantially reduce the lipase and lipoxygenase activity of the coarse fraction without substantial gelatinization of the starch. High levels of natural antioxidants and vitamins are retained while avoiding substantial acrylamide formation during the stabilization. The stabilized coarse fraction or stabilized bran component may be combined with a fine fraction which contains predominantly endosperm to obtain a stabilized whole grain flour. The stabilized whole grain flours and the stabilized bran component exhibit extended shelf life and may be used for making baked goods, such as cookies, with desirable oven spread, and a non-gritty mouthfeel.

Production of stabilized whole grain flour and products thereof

A stabilized bran component and stabilized whole grain wheat flour containing the component are produced by subjecting a bran-enriched coarse fraction which contains bran, germ and starch to grinding or milling to reduce grittiness of the coarse fraction without substantially damaging the starch due to abrasion. The coarse fraction may be stabilized by heating to substantially reduce the lipase and lipoxygenase activity of the coarse fraction without substantial starch gelatinization. High levels of natural antioxidants and vitamins are retained while avoiding substantial acrylamide formation during the stabilization. The stabilized coarse fraction or stabilized bran component may be combined with a fine fraction which contains predominantly endosperm to obtain a stabilized whole grain wheat flour. The stabilized whole grain wheat flours and stabilized bran component exhibit extended shelf life and may be used for making baked goods, such as cookies, with desirable oven spread, and a non-gritty mouthfeel.

Production of stabilized whole grain wheat flour and products thereof

A method for the continuous production of sandwich baked goods having a high volume of filler includes conveying a bottom base cake, detecting the position of the base cake, and extruding a filler through a die aperture to form a ribbon in response to the detection of the position of the bottom base cake. In response to detection of the base cake, a signal or timing mechanism may activate a guillotine knife or blade to open the die aperture to allow filler to be deposited on the bottom base cake and to close the die aperture to sever or cut the ribbon to a predetermined dimension. The severing prevents further flow of the filler through the die aperture until the next bottom base cake is detected and the die aperture is again opened to allow filler to be deposited on the next bottom base cake.

Ribbon cutter apparatus and method for making sandwich baked goods

A cookie cup sandwich cookie having dissimilarly-sized base cakes is continuously produced by applying a layer of filler cream to a lower base cake and applying an upper base cake to the lower base cake so that the outer periphery of the upper base cake surrounds the layer of filler cream. The apparatus for the production of the sandwich cookies includes at least one rotary molder for producing lower base cakes and upper base cakes having different sizes, a filler cream depositor that deposits a layer of filler cream on each of the lower base cakes, and a conveyer system for transporting and at least substantially concentrically aligning the dissimilarly sized lower and upper base cakes.

Method for producing sandwich cookie having dissimilarly-sized base cakes

Shredded whole grain products, such as ready-to-eat cereals, and sweet and savory snacks, such as whole grain shredded corn chips are continuously produced by pelletizing agglomerates of cooked, tempered, whole cereal grain particles. Cooked whole grains, such as corn and other non-gluten or low-gluten containing grains have a tendency to become hard and rubbery after cooking during the cooling and tempering process. The pelletization results in the production of whole grain pellets having a soft, pliable texture, which are shreddable into continuous net-like sheets on a mass production basis. The pelletizing may be at a pressure of about 200 psig to about 600 psig, preferably from about 400 psig to about 500 psig. The pelletizing temperature may be controlled to provide a pellet temperature of about 80&#xb0; F. to about 135&#xb0; F., preferably from about 90&#xb0; F. to about 110&#xb0; F., upon exiting the pelletizer.

Growing community of inventors

Palisades Park, NJ, United States of America

Mihaelos N Mihalos