Sausage casings

Abstract

The invention is directed to a process for preparing a food casing, in particular a sausage casing. The sausages thus produced can be dried more efficiently because of the higher initial solids content of the casing, after they leave the extruder.

Claims

1. A co-extrusion process for preparing a food casing, comprising: preparing a collagen water mixture by adding a salt to the collagen water mixture, wherein the concentration of collagen in said mixture is 6-10 wt. %, wherein said salt is sodium chloride and is present in said mixture in a concentration of about 0.1 to about 0.7 mol/dm.sup.3 followed by a subsequent acidification step, thereby forming a gel, followed by a co-extrusion step wherein said casing is formed from said gel, via a co-extrusion process, wherein said salt reduces swelling of collagen fibers upon said acidification; and wherein said gel has a viscosity of less than 20,000 cP.

2. The process of claim 1, wherein said salt is present in said mixture in a concentration of about 0.15 to about 0.35 mol/dm.sup.3.

3. The process of claim 1, wherein said salt is present in said mixture in a concentration of about 0.22 mol/dm.sup.3.

4. The process of claim 1, wherein a concentration of the collagen in said mixture is about 8 weight %.

5. The process of claim 1, wherein said gel has a viscosity in a range of about 12,000 to about 19,000 cP.

6. The process of claim 1, wherein said gel has a viscosity in a range of about 12,000 to about 16,000 cP.

7. The process of claim 1, wherein the food casing is a sausage casing.

Description

BRIEF DESCRIPTION OF THE DRAWING FIGURES

(1) FIG. 1 schematically depicts a co-extrusion process for making a sausage.

DETAILED DESCRIPTION

(2) Thus, in a first aspect the present invention relates to a process for preparing a food casing, comprising the steps of preparing a collagen water mixture, which further contains salt, followed by a subsequent acidification step, thus forming a gel, followed by a step wherein said casing is formed. The sausages produced in accordance with the invention can be dried more efficiently because of the higher initial solids content of the casing, after they leave the extruder.

(3) The acidification step can be carried out using for instance lactic acid, acetic acid or combinations thereof.

(4) Preferably the salt, which is preferably an alkali halide, more preferably sodium chloride, is present in the collagen/water mixture in an amount of about 0.05-1 mol/dm.sup.3, more preferably about 0.1-0.7 mol/dm.sup.3, even more preferably about 0.15-0.35 mol/dm.sup.3, for instance 0.22 mol/dm.sup.3. These amounts were found to give good results with respect to swelling behavior.

(5) The salt according to the present invention may reduce the swelling of collagen fibers upon acidification and as such the higher protein concentration does not increase the viscosity of the resulting collagen gel. Polysaccharide salts, such as pectinate and/or alginate salts (e.g. sodium alginate and/or sodium pectinate) typically increase the viscosity of the resulting gel and are therefore not preferred. Hence, the salt according to the present invention is preferably a salt other than an alginate salt and/or pectin salt (pectinates), more preferably a salt other than a salt of a polysaccharide.

(6) The amount of collagen present in the collagen/water mixture is preferably more than 4 wt. %, more preferably more than 5 wt. %, even more preferably 6-10 wt. %. a collagen concentration of about 8 wt. % was found to be very suitable.

(7) The resulting gel generally has a viscosity of less than 20 000, typically about 12 000-19 000 cP, preferably about 12 000-16 000 cP, which can be extruded very well in existing extruders.

(8) In accordance with the present invention sausages are prepared by applying the casings obtained from the gel described above in the usual manner, for instance using the coextrusion process described in Meatprocessing, February (1982)30-36.

(9) Another advantage of the gel according to the present invention, is that a higher collagen concentration in the gel allows for a lower amount of gel to be used in the co-extrusion of the sausages. This may lower the total cost of the production of sausages.

(10) In a typical co-extrusion process for making sausages is shown schematically in FIG. 1. The collagen gel (also sometimes referred to as collagen dough is fed in a cone-shaped nozzle of an extruder, as indicated by arrow 1. The meat batter (4) is fed through the center of the nozzle, as indicated by arrow 2. It passes a venturi (5). Then the collagen stream (3) is directed to the outside of the sausage and forms the socalled sausage rope 6. After leaving the extruder the sausage thus formed is typically passed through a saturated salt solution (typically sodium chloride), typically for about 2 seconds. It is then cut to the required length and deposited on a stainless steel supporting belt and exposed to hot air. Typically the hot air has a temperature of about 100 C.

(11) Wet collagen is irreversibly converted to gelatin at relatively low temperatures, for instance already at 40 C. or above. In the prior art, at the position where the sausage surface contacts the supporting grid gelatinization may occur resulting in marks and/or indentations in the sausage surface. Due to the higher initial solids content of the skin produced in accordance with the present invention the drying temperature can be decreased without loosing production capacity and indentations will be less perceivable. After drying the food products, in particular sausages, obtainable by the process of the invention are characterized by the absence or substantial absence of any burn marks and/or indentations that would result from heating too long on a gridiron in the drying oven.

EXAMPLES

Example 1 (Reference)

(12) A collagen gel was prepared by mixing bovine collagen fibers (4 wt. %) with water, acidifying the mixture to a pH of 3 with lactic acid and homogenizing. The acidification resulted in swelling of the collagen fibers, thus producing the collagen gel. The gel was used to prepare collagen coated sausages by coextrusion. The resulting sausages were dried in a conventional oven with hot air of 100 C. The sausages were heated to a temperature of 60 C. for a period of 12 minutes. This resulted in part of the sausages showing burnmarks on the outer surface in the form of dark stripes, which corresponded to the gridiron.

Example 2 (Reference)

(13) Example 1 was repeated, but the amount of collagen in the mixture was increased to 8 wt. %. The resulting gel after acidification was too viscous to be processed by the extruder. No sausage could be made.

Example 3

(14) Example 2 was repeated but now NaCl was added to the mixture, prior to the acidification step. The ingredients were thoroughly mixed. The amount of NaCl used was 0.22 mol/liter. After acidification the resulting gel was clearly less viscous than in Example 2 and could be properly extruded. The resulting cases were used to prepare sausages as described in Example 1. The sausages were subsequently dried to the same surface dryness water content. The required drying time was reduced by 25%. In an alternative test the sausages were dried at 80 C. in the same time as in Example 1 (12 minutes). The sausages had the same surface dryness in spite of the shorter time. The resulting dried sausages did not show any marks after the drying step.

Example 4

(15) Example 3 was repeated but now 7 wt. % bovine collagen fibers and 1.20 wt. % NaCl were mixed with water. The resulting collagen gel had a viscosity of 19.000 cP.

(16) The resulting cases were used to prepare sausages as described in Example 1. The rheological properties of the collagen gel were similar to the collagen gel obtained in Example 1. Thus a well distributed coverage of the collagen gel on the sausage and a non-pulsating string of sausages extruded by the coextruder were obtained. The amount of collagen gel on the sausages was reduced to 70% and the required drying time was reduced to 80% compared to Example 1.