This invention relates to the use of agglomerated/freeze dried milk powder in beverage such as coffee and tea as an alternative to artificially made coffee whiteners and liquid milk.
The concept of using liquid milk in coffee and tea has been prevalent for over a hundred years.
The use of milk substitutes in powder form for coffee originated about 40 years ago. These milk substitutes made as “coffee-whiteners” were formulated with corn syrup solids, hydrogenated oils (for fat), artificial coloring and preservatives. However, ironically nobody has applied the direct use of dry milk powder in coffee or tea.
There are several reasons for this:
Dry Milk Powder, agglomerated or otherwise as presently available in Bulk or consumer packaging is used primarily for reconstitution, baking, mixing or confectionary needs. No application has been developed or used for purposes of using the milk powder 100% directly in vending machines for beverage purposes.
The removal of water from milk can result in various dairy ingredients, from condensed milk, to cream, to butter, to whole milk and skim powder. Also, the removal of water from milk offers the manufacturer significant reduction in volume (about 87% of all milk is water), which not only saves in handling and transportation costs but extends the life of the products as much as 18 months, when packaged appropriately.
Over the years as the technology of evaporating and spray drying has evolved from transforming liquid ingredients into a dry powdered form or particle form, so have the applications of using these products.
It is not only milk that is spray dried, but hundreds of other products are also spray dried including eggs; ice cream mixes; coffee whiteners; soy powders and various fruits and vegetables.
The inventor has recognized the advantages of this dry powder technology; particularly where it pertains to milk and the subsequent use of “agglomeration or instantization technology” to enable the dry powdered product to be more soluble and easily dispersible, so that it may be applied in beverages such as coffee and tea as a substitute for liquid milk and non-dairy whiteners.
To accomplish the invention, dry milk powder is obtained from whole milk or skim milk. To obtain skim milk powder, the whole milk is first separated to take out the fat (cream). It is then pasteurized and pumped to an evaporator to remove the water, which condenses the milk to 40% to 50% solids.
From there it is pumped to a spray dryer, where the remaining water is dried (ideal moisture of 2.8% to 3.5%) and the product is dried to powder form.
In order to achieve the right solubility and uniform particle size to mix in beverages such as coffee and tea without lumping or floating the milk needs to be further processed, such as in a two stage dryer or a separate agglomerator.
In this second drying chamber (known as a fluid bed system or agglomerator) air volumes, moisture, and temperatures can be controlled to achieve the desirable composition and functional properties of the powder.
This second stage of drying is called “agglomeration” or “instantizing” of the powders. Agglomeration reduces powder surface area, and provides an open, heavier structure which allows for more even hydration. An agglomerated product offers better and faster dispersion when it is introduced into beverages.
When applied through this production process, using controlled air volumes, moisture and temperatures one is able to achieve a product that when mixed with water dissolves essentially instantly. It is this use of the agglomeration technology when applied to milk that enables the dry milk powder to not only be easily reconstituted for drinking purposes, but can be marketed as “Real Milk” for the use in beverage and vending purposes. There remains no lumping or floating of product versus if it was only spray dried in a single system. It is also a much more free flowing product that does not bridge or cake when dispensed through automatic vending machines.
The inventor has further identified that non fat dry milk powder when manufactured and agglomerated should have a particle bulk density between 0.25 g/cc and 0.34 g/cc; with ideal initial bulk density of 0.28 g/cc; combined with the other controlled factors it is most easily dispersible and free flowing for purposes of adding to a hot beverage whether through a vending machine or directly.
The final product ideally should have moisture ratio of between 2.8% to 3.5%, and scorched particles mass between 7.5 mg and 15.0 mg. A higher scorched particle mass will result in floaters in the beverage and like lumping will be considered adversely by the consumer.
Therefore, a main objective of this invention is to introduce an ideally manufactured agglomerated milk powder that is easily soluble and dispersible for use in automatic vending machines and applicable as an alternative to liquid milk and non dairy powders for use in hot beverages.
These and other objects and features of the invention will be more readily understood from a consideration of the following detailed description, taken with the accompanying drawings, in which corresponding parts are indicated by corresponding numerals.
In order to practice the instant invention, it is preferred to agglomerate or instantize liquid milk.
It is widely accepted that liquid milk has a shelf-life of on the order of only two weeks, and that dried powdered milk has a shelf-life of up to two years if packaged appropriately.
When it comes time to use the dried powdered milk, the solubility thereof in a beverage is critical to the desirability of the product to the consumer. It is, therefore, preferred that in the processing of the liquid milk into a dried powder, the product be agglomerated or instantized. One way of accomplishing this is through the use of a multi-stage dryer. In a first stage, a spray dryer is used, and in a second stage a fluid bed dryer is employed. Spray drying involves transferring a flowable medium such as liquid milk into a drying chamber, where the liquid droplets are passed through a hot air stream. The objective is to produce a spray of high surface area to mass ratio droplets (ideally of equal size), then to uniformly and quickly evaporate the water. Non-agglomerated powder particles are shown at “A” to the left in
In an exemplary embodiment, the multi-stage dryer may include a spray dryer in a first stage 42 and a fluid bed dryer in a second stage 44. However, it is contemplated to be within the scope of the invention that any apparatus and/or procedure which results in agglomerated power can be used, and that the specific apparatus and procedures recited herein are done so by way of example and not by way of limitation. The result of the multi-stage process 40 is an agglomerated or instantized powder which can be either packaged or dispensed via a vending machine for consumer consumption. The specifics of agglomeration and instantization, and alternatives and variations thereof, are known to those who are skilled in the art and need not be discussed further herein. It is to be understood, however, that agglomerated product is preferred, since agglomeration reduces powder surface area, and provides an open, heavier structure which allows for more even hydration. The particles sink below the surface of the liquid, such as a beverage, and break apart, allowing smaller particles within the agglomerate to completely hydrate. This means better and faster dispersion within a beverage. While individual powder particles of typical food products are usually less than 100 microns, agglomerates are typically 250 to 400 microns. Bulk density decreases from approximately 42 pounds per cubic foot to approximately 28 pounds per cubic foot.
The agglomerated powdered milk is then packaged, transported through a distribution network and placed into automated vending machines (shown as step 50) to be dispensed on demand at step 60 with various beverages, such as coffee, tea, cappuccino and hot chocolate.
The procedure for this example repeats the steps detailed in Example 1 but interposes the intermediate step 53, shown in
The procedure of
The agglomerated natural milk powder resulting from step 44 can be placed into any suitable container such as a consumer package for transportation and retail sale or other disposition. Moreover, as shown in
This application is a division of co-pending U.S. patent application Ser. No. 10/877,469 filed Jun. 25, 2004, currently pending, which is a continuation of U.S. patent Application Ser. No. 09/898,968 filed Jul. 3, 2001 and issued on Aug. 17, 2004 as U.S. Pat. No. 6,777,014 B2.
Number | Date | Country | |
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Parent | 10877469 | Jun 2004 | US |
Child | 11214703 | Aug 2005 | US |
Number | Date | Country | |
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Parent | 09898968 | Jul 2001 | US |
Child | 10877469 | Jun 2004 | US |