Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Method and apparatus for producing fully cooked extrudates with significantly reduced specific mechanical energy inputs

a technology of specific mechanical energy and extruder, which is applied in the direction of feeding-stuff, application, manufacturing tools, etc., can solve the problems of increasing utility costs, limiting the steam of conventional extrusion systems, and affecting the quality of extruder components, so as to reduce the sme input, the effect of reducing the sme input and reducing the cos

Inactive Publication Date: 2010-03-11
WENGER MANUFACTURING INC
View PDF0 Cites 27 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The solution significantly reduces SME inputs, lowering equipment costs and energy consumption, enabling the production of fully cooked and expanded products with improved cook values and expansion characteristics, while maintaining product quality and reducing wear on extruder components.

Problems solved by technology

Conventional extrusion systems are limited in the amount of steam which can be injected into the extruder barrel, typically no more than about 5% by weight.
Consequently, the extrusion equipment must have a more robust and therefore construction than would otherwise be necessary, the extent of extruder component wear is higher than desirable, and utility costs are increased.
Skilled artisans understand that a ratio of 1.3 is too small, in that the screw(s) lack free volume, creates excessive shear inputs and consumes too much power.
Similarly, a ratio above 1.8 is deemed too large, in that the screw has too much free volume and which will prevent barrel fill and the ability to achieve a desired cook value.
Any significant axial gap or clearance between the adjacent flighting sections is considered to be detrimental in that it could create dead zones of accumulated product, and also would decrease the extent of product mixing within the extruder barrel.
However, these types of extruders will be deficient in that cook values will be unacceptably low and significant expansion cannot be achieved.
Alternately, an aggressive extruder design can be used, which will assure adequate cook and expansion of products, but this will inevitably result in high shear and SME inputs with resultant higher costs.

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Method and apparatus for producing fully cooked extrudates with significantly reduced specific mechanical energy inputs
  • Method and apparatus for producing fully cooked extrudates with significantly reduced specific mechanical energy inputs
  • Method and apparatus for producing fully cooked extrudates with significantly reduced specific mechanical energy inputs

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0058]In these illustrative tests, data from a previous run using a Wenger Magnum ST TX85 twin screw extruder was compared with the improved twin screw extruder of the invention, in the preparation of aquatic feeds. The TX85 extruder is of the type illustrated in FIGS. 10-11 whereas the extruder of the invention is illustrated in FIGS. 1-5. As can be seen, both extruders include shorter pitch sections located on opposite sides of longer pitch steam injection sections. In the case of the TX85, the injectors were located in perpendicular relationship to the longitudinal axes of the extruder screws, whereas in the improved extruder, the injectors were oriented at a 45° angle relative to the screw axes. Moreover, the twin screws of the TX85 had a close flighting-to-flighting gap of about 0.039 inches along the entire lengths thereof, and the longer pitch sections thereof had a significantly smaller flighting depth (measured from the outer surface of the flighting to the shaft) and a con...

example 2

[0066]In this set of tests, essentially the same extruder set-ups were employed, with no steam injection to the TX85 extruder, but with a maximum amount of steam injection to the improved extruder hereof, The TX85 equipment did not include a BPV.

[0067]The recipe used with the TX85 (No. 3) was a proprietary pet food recipe, whereas the recipe in the improved extruder (No. 4) was the same as that set forth in Example 1. The data collected in this set of runs is set forth in the following Table 3.

TABLE 3RUN NUMBER34DRY RECIPE INFORMATIONDensity (kg / m3)551608Feed Rate (kg / hr)11852000Feed Screw Speed (RPM)2540PRECONDITIONING INFORMATIONPreconditioner Speed (RPM)125 / 25050 / 800Steam Flow to Preconditioner (kg / hr)120160Steam Flow to Preconditioner (%)108Water Flow to Preconditioner (kg / hr)125280Water Flow to Preconditioner (%)10.514Weight in Preconditioner (kg)82122Preconditioner Retention Time (min)3.372.69Preconditioner Discharge Temp (° C.)9281Moisture Entering Extruder (% wb)—25.02EXTRUS...

example 3

[0069]In this example cat food products were prepared using the basic extruder assembly of FIGS. 1-5 and the preconditioner of FIGS. 8-9. The objective of these tests was to prepare a light density (320-350 g / l, or about 20-22 lb / ft3) cat food using less than 10 kWhr / T SME input with 12% by weight steam injection into the extruder barrel. The dry ingredient recipe was made up of 53% by weight corn, 22% by weight poultry meal, 15% by weight soybean meal, and 10% corn gluten meal. This recipe provided 32.6% by weight protein, 4.0% by weight starch, 34.9% by weight fat, and 2.9% by weight fiber. The results of this run are set forth in Table 4.

TABLE 4ProductCat FoodRUN NUMBER567DRY RECIPE INFORMATIONDensity (kg / m)556556556Feed Rate (kg / hr)200020002000Feed Screw Speed (RPM)404040PRECONDITIONING INFORMATIONPreconditioning Speed (RPM)50 / 80050 / 80050 / 800Steam Flow to Preconditioner (kg / hr)166166166Steam Flow to Preconditioner (%)8.38.38.3Water Flow to Preconditioner (kg / hr)114114114Water Fl...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
angleaaaaaaaaaa
angleaaaaaaaaaa
angleaaaaaaaaaa
Login to View More

Abstract

Improved extruders and methods for the extrusion cooking of comestible products such as human foods or animal feeds are provided wherein the products may be produced with very low specific mechanical energy (SME) inputs as compared with conventional processing. The methods preferably involve introduction of very high levels of steam into the extruder barrel (12) during processing, which concomitantly reduces necessary SME inputs required to achieve desired cook and expansion levels in the products. In accordance with the invention, fully-cooked pet foods can be fabricated with SME inputs of up to about 18 kWhr / T, whereas aquatic feeds can be fabricated with SME inputs of up to about 16 kWhr / T. In preferred forms, the extruder (10) includes specially configured, intermeshed extrusion screws (18, 20) and a plurality of obliquely oriented steam inlets (48, 50), and an upstream, dual-shaft preconditioner (90) is used having individual variable frequency drives (98, 100) which allow infinite variablility in the speed and rotational direction of the preconditioner shafts (94, 96).

Description

BACKGROUND OF THE INVENTION[0001]1. Field of the Invention[0002]The present invention is broadly concerned with improved extruders and methods for extrusion processing of comestible products with very low specific mechanical energy (SME) inputs as compared with conventional methods. More particularly, the invention is concerned with extruders having specially configured screws designed to permit addition of very high quantities of steam, so that the amount of SME required to for complete cooking is maritally reduced. The resultant feeds have very high cook values and expansion characteristics.[0003]2. Description of the Prior Art[0004]Extrusion processing of comestible products such as human foods and animal feeds has long been practiced and is a highly developed art. In general terms, food extruders of the single or twin screw variety are employed, having elongated, tubular barrels with inputs adjacent one end thereof and restricted orifice dies at the outlet thereof, and one or tw...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(United States)
IPC IPC(8): A23P1/12B29C48/03B29C48/06B29C48/295B29C48/395B29C48/40B29C48/405B29C48/535B29C48/54B29C48/80
CPCA23N17/005B29C47/1072B29C47/0016B29C47/38B29C47/402B29C47/80B30B11/243B30B11/246B29C47/666B29C47/6031B29C47/0009B29C47/0805B29C47/6025B29C2947/9259B29C2947/92885B29C2947/92952A23P1/12A23P30/20B29C48/03B29C48/2526B29C48/295B29C48/535B29C48/832B29C2948/9259B29C2948/92885B29C2948/92952B29C48/06B29C48/54B29C48/395B29C48/402B29C48/405B29C48/40Y02P70/10B29C48/80B29C48/686
Inventor WENGER, LAVONWENGER, MARCROKEY, GALEN J.SPELLMEIER, ALLAN C.
Owner WENGER MANUFACTURING INC
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products