Process to obtain a round shaped collagen casing and casing obtained by the process

Abstract

The present invention relates to a process to obtain a round shaped collagen casing and to the casing obtained by the process, which is based on a post rounding of a straight collagen casing by controlled heat shrinking.

Claims

1. A process to obtain a round shaped collagen casing comprising the steps of: a) guiding a straight inflated collagen casing which has a humidity between 12% to 30% balanced to a total weight of the casing and contains collagen plasticizer between 12% to 24% balanced to the total weight of the casing and an inside gas pressure between 20 mbar to 700 mbar to a heat transfer unit; b) transferring heat energy to the casing by the heat transfer unit to obtain a round shaped collagen casing, wherein a temperature achieved in an innermost ring of the casing is higher than a shrinkage temperature of the collagen casing; and, c) supporting the round shaped collagen casing by a round element.

2. The process according to claim 1 wherein the straight inflated collagen casing has a humidity between 15% to 25% balanced to the total weight of the casing.

3. The process according to claim 1 wherein the straight inflated collagen casing contains collagen plasticizer between 14% to 22% balanced to the total weight of the casing.

4. The process according to claim 1 wherein the plasticizer is glycerol.

5. The process according to claim 1 wherein the heat transfer unit is a blower.

6. The process according to claim 1 wherein the round element is a thermoregulated round element.

7. The process according to claim 1 wherein the inflated collagen casing is embraced around a roller at least to ¼ of a circle, and the roller is maintained at a temperature between room temperature to the shrinkage temperature of the collagen casing.

8. A round collagen casing obtained by the process defined in claim 1.

9. A collagen casing characterized by a round shape wherein a ratio of longitudinal outer ring shrinkage/longitudinal inner ring shrinkage is higher than 1.25.

10. A collagen casing obtained by the process of claim 1 characterized by a round shape wherein a ratio of longitudinal outer ring shrinkage/longitudinal inner ring shrinkage is higher than 1.25.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) For the purpose of aiding the understanding of the characteristics of the invention, according to a preferred practical embodiment thereof and in order to complement this description, the following figures are attached as an integral part thereof, having an illustrative and non-limiting character:

(2) FIG. 1 schematically illustrates an exemplary design of the inventive post rounding method.

(3) FIG. 2a illustrates the inflated casing tube before its heat shrinking.

(4) FIG. 2b illustrates the inflated casing tube after its transformation to a post rounded casing by heat shrinking.

(5) FIG. 3 explains the expressions for describing the post rounded casing.

DETAILED DESCRIPTION OF THE INVENTION

(6) As mentioned above an aspect of the invention refers to a process to obtain a round shaped collagen casing comprising the steps of:

(7) a) guiding a straight inflated collagen casing which has a humidity between the 12% to the 30% balanced to the total weight of the casing and contains collagen plasticizer between 12% to 24% balanced to the total weight of the casing and an inside gas pressure between 20 to 700 mbar to a heat transfer unit;

(8) b) transferring heat to the casing by a heat transfer unit to obtain a round shaped collagen casing, wherein the temperature achieved in the innermost ring of the casing is higher than the shrinkage temperature of collagen casing;

(9) c) supporting the round shaped collagen casing by a round element.

(10) Preferably the straight collagen casing is any non-crosslinked or chemically or physically (e.g. thermally or UV) crosslinked straight collagen casing extruded out of bovine, porcine, ovine or any other fibrous collagen resource, including their mixtures.

(11) The straight casing can be post rounded directly at the end of the production dryer prior to inline shirring or separately from reel to reel.

(12) Preferably the distance between the heat unit and the innermost ring and the outermost ring is different. Preferably the heat transfer unit is selected from a blower or a temperature regulated wheeler. Preferably the round element is a thermoregulated round element. Preferably the round element is selected from: a roller or a wheeler. In a particular embodiment the heat transfer unit and the round element is the same thing and it is a temperature regulated wheeler.

(13) When the heat transfer unit and the round element are not the same and the round element is a roller, more preferably the roller is maintained at a temperature between room temperature to the shrinkage temperature of the collagen casing and the inflated collagen casing is embraced around a roller at least to ¼ of a circle.

(14) In an embodiment of the present invention the humidity of the straight inflated collagen casing is between 15% to 25% and more preferably is between 17.5% to 22.5% balanced to the total weight of the casing. More preferably the straight inflated collagen casing contains collagen plasticizer, between 14% to 22% and more preferably between 16.5% to 20% collagen plasticizer, balanced to the total weight of the casing. Particularly preferred the collagen plasticizer is glycerol.

(15) Preferably the inflated collagen casing have an inside gas pressure between 50 to 400 mbar and more preferably 75 to 300 mbar.

(16) When straight inflated collagen casing which has a humidity between the 12% to the 30% balanced to the total weight of the casing and contains collagen plasticizer between 12% to 24% and an inside gas pressure between 20 to 700 mbar, very reliable is the measurement of longitudinal heat shrink of a 5 mm wide stripe directly cut in the machine direction from the innermost and the outermost ring periphery of the post rounded casing measured at 80° C. in water. The inner ring stripe heat shrinks hereby far less than the outer ring stripe obeying the equation:
Longitudinal outer ring shrinkage/Longitudinal inner ring shrinkage>1.25
Corresponding casing stripes cut out of a round shaped collagen casing produced according to conventional method shows similar behaviour however more outbalanced always fulfilling the equation:
Longitudinal outer ring shrinkage/Longitudinal inner ring shrinkage<1.25.
Longitudinal heat shrink of the post rounded casing is measured according to the method described in IUP-Norm Nr. 16: Leder 15, 85 (1964) enclosed here by reference.

(17) Therefore another aspect of the invention is collagen casing with a round shaped wherein the ratio, longitudinal outer ring shrinkage/longitudinal inner ring shrinkage is higher than 1.25.

(18) In the FIG. 1 a particular process to obtain a round shaped collagen casing is described.

(19) A straight collagen casing from a mother reel (1) or directly from the production dryer (2) is guided by means of the conveyor pair of rollers (3) through a water ring sprayer (5) and a ring blower (6), which is fed with heated air, not shown. The thermo regulated roller (7) builds together with the flattening small roller (8) the uptake pair of rollers. The starting straight collagen casing may be already adjusted to the requested humidity or it may be inline re-humidified by passing the water ring sprayer (5).

(20) A permanently captured inflated casing bubble (4) is maintained between the conveyor pair of rollers (3) and the uptake pair of rollers, thermo regulated roller (7) and small roller (8). The conveying pair of rollers (3) is designed for axial back and forward movement commanded by a diameter laser measuring unit, not shown, to regulate the inflation pressure and consequently the calibre of the straight casing prior to post rounding. The inflated casing bubble (4) is embraced around the thermo regulated roller (7) having an outside diameter up to 750 mm, preferably up to 350 mm and especially between 65 mm and 200 mm, at least to ¼ of a circle, preferably to ⅘ and optionally to one or more turns of a circle.

(21) Both conveyor pair of rollers (3) and thermo regulated roller (7) and small roller (8) are then started to rotate. Pressurised air heated to a temperature above the shrinking temperature of collagen is circumferentially directed along (4) through the air ring blower (6) directly positioned in front of the roller (7), which is internally thermo regulated by continuous water circulation, not shown in detail. The air ring blower (6) and the casing bubble (4) are excentrics. The air ring blower (6) can be optionally assisted by additional heated air blower, directed to the flanks while the casing bubble (4) is embraced around the thermo regulated roller (7). Passing the air ring blower (6) the inflated casing bubble (4) heat shrinks along its inner ring periphery and becomes hereby post rounded. The post rounded casing is then further conveyed as finished product, that is the post rounded casing (9) to the reeling unit (10) or directly into the shirring machine (11).

(22) The smaller the diameter of stainless steel thermoregulated roller (7), the smaller is the inner ring diameter (15) of the resulting post rounded casing (9). The surface temperature of the thermoregulated roller (7) is maintained between room temperature and the shrinking temperature of the starting casing.

(23) Higher inflation pressure inside the casing bubble (4) minimises the inner ring diameter (15) of the post rounded casing (9) equalising it more and more to the diameter of the thermoregulated roller (7). Decreased inflation pressure in the casing bubble (4) consequently increases the inner ring diameter (15) of the resulting post rounded casing (9).

(24) Contact time between the casing bubble (4) and the thermoregulated roller (7) determines the post rounding speed. Longer contact time allows faster post rounding and vice versa. Maximum embracing of the casing bubble (4) around the thermoregulated roller (7) is preferred.

(25) The temperature of the air flow through the air blower(s) (6) is always higher than the shrinkage temperature of the casing. It is however adjusted as low as possible to avoid excess heat degradation of the post rounded collagen casing (9).

(26) The effective distribution of the heated air circumferentially around the casing bubble (4) is best achieved by positioning of the air ring blower (6) as close as possible to thermoregulated roller (7) as shown in FIG. 1. The flow rate of the heated air must be sufficient to actuate heat shrinking of the casing bubble (4).

(27) The inner ring diameter (15) of the resulting post rounded casing (9) increases, when the uptake rollers, thermo regulated roller (7) and small roller (8) rotate faster and vice versa. Uptake rollers, thermo regulated roller (7) and small roller (8) however rotate principally slower than the conveyor pair of rollers (3) for realising post rounding.

(28) Heavily crosslinked collagen casings require higher air temperatures blown trough the air blower (6) for heat shrinking and vice versa. Too high shrinking temperatures however should be principally avoided to avoid excess collagen degradation during post rounding.

(29) The inventive method can be optimised according to these teachings by average researchers without leaving the frame of the present invention.

(30) Some of the advantages of the present invention are: the process is carried out in a compacted rounding unit can be installed in line to the straight casing production or separately offline demanding only a limited space compared to the previous techniques. The energy demand of the process described in the present invention is minimised. Production logistics are extremely simplified, because mother reels of straight collagen casing are standard almost in all calibres. Deliveries to customers are therefore accelerated. The complex rotating segments of the conventional method requiring intensive maintenance and multiple man power are replaced by a simple and fully automated post rounding unit as exemplary shown in FIG. 1. No collagen is “rubbed off”, therefore post rounded collagen casings having a thinner wall thickness can be produced, offering improved bite and chewing properties. The overall performance of the casings is improved, because it is no more limited by the specific technique of the prior conventional method.

(31) In the following examples the invention is described in more detail however the invention is not limited by them.

EXAMPLES

Comparative Example A

(32) The commercially marketed SCC calibre 21 of Viscofan S.A./Spain, according to the US patent specification 6,436,456 is a conventionally produced round shaped artificial collagen. It is selected for comparison purposes with the inventive examples 1 and 2.

Comparative Example B

(33) Commercially available natural Sheep Saitling code A calibre 20/22 is further selected for comparison purposes with the inventive examples 1 and 2.

Comparative Example C

(34) The commercially marketed “Kranzdarm” calibre 39 of Viscofan S.A./Spain is a conventionally produced round shaped non edible artificial casing. It is selected for direct comparison with the post rounded “Kranzdarm calibre 39” according to the inventive example 3.

Example 1

(35) A straight collagen NDX casing calibre 21, commercialised by Viscofan S.A./Spain, having 22% humidity and 17% glycerol as plasticiser balanced to its total weight is post rounded as by heat shrinking.

(36) The mother reel of the chemically crosslinked NDX casing (1) is manually reeled off, conveyed through the conveyor pair of rollers (3) and further through the air ring blower (6) around the thermo regulated roller (7) to the uptake pair of rollers built by the thermo regulated roller (7) and the small roller (8) as illustrated in FIG. 1.

(37) The NDX casing is air inflated to 200 mbar and its bubble is captured between the conveyor pair of rollers (3) and the pair of rollers formed by the thermo regulated roller (7) and the small roller (8). The casing bubble (4) is next tightly embraced to ¾ around the thermo regulated roller (7) having a diameter of 115 mm. The casing bubble (4) hereby forms radial buckles (12) along its innermost ring (13) as shown in FIG. 2a.

(38) A diameter laser, not shown in FIG. 1, regulates the desired inflation diameter of the captured casing bubble (4) to 20.80 mm by moving the platform carrying the conveyor pair of rollers (3) forward and/or backward.

(39) The conveyor pair of rollers (3) are rotated at 13.3 meters/minute and the uptake pair of rollers built by the thermo regulated roller (7) and the small roller (8) are rotated at 10 meters/minute. Sufficient air flow, heated to 82° C. is circumferentially blown through the air ring blower (6) around the inflated casing bubble (4) just before it contacts the thermo regulated roller (7).

(40) The thermo regulated roller (7) is thermo regulated to 40° C. by circulating warm water inside. Additional air flow of 82° C. can be specifically directed against the rings of the casing bubble (4) embracing the thermo regulated roller (7) by means of a U-shaped air blower not shown in detail.

(41) The captured casing bubble (4) heat shrinks hereby along its innermost ring (13), becomes continuously rounded, while its radial buckles (12) disappear as shown in FIG. 2b. The rounded casing is flattened and uptake by the thermo regulated roller (7) and the small roller (8). The resulting post rounded casing (9) is then further conveyed to the reeling unit (10) or alternatively into the inline shirring machine (11).

(42) The inner ring diameter (15) of the resulting post rounded casing measures 165 mm and its calibre 17 20.8 mm, when it is re-inflated to 200 mbar.

(43) Simple visual check does not show any “rubbed off” collagen.

(44) Two 5 mm wide longitudinal stripes directly cut out of the innermost and outermost ring periphery of the post rounded casing are heat shrunk in hot water at 80° C. according to the method described in IUP-Norm Nr. 16: Leder 15, 85 (1964).

(45) Longitudinal outermost ring shrinkage: Sor

(46) Longitudinal innermost ring shrinkage: Sir

(47) Sor/Sir=1.364

(48) The resulting post rounded casing of this inventive example 1 is directly compared with the casings of the comparative examples A and B:

(49) Sor/Sir=1.19

(50) The innermost ring shows the typical appearance of “rubbed off” collagen.

Example 2

(51) A reel of straight collagen casing Colfan B calibre 19, commercialised by Viscofan S.A./Spain is post rounded by applying the same technique described in the inventive example 1.

(52) TABLE-US-00001 Croslinking thermally crosslinked Humidity 21% balanced to the total weight Glycerol 16% balanced to the total weight Inflation pressure 150 mbar Inflated calibre laser reading 17.9 mm Diameter of the stainless steel 130 mm roller 7 Hot air temperature for post 75° C. rounding blown through 6 Outside surface temperature of 35° C. stainless steel roller 7 Post rounding speed 20 m/min. Inner ring diameter of the post 150 mm rounded casing 15 Inflated calibre of the post 17.8 mm rounded casing 17

(53) No collagen is “rubbed off”.

(54) TABLE-US-00002 Sir/Sor 1.35
The resulting post rounded casing of inventive example 2 is further compared with casings of the comparative examples A and B:

(55) Clear visual detection of “rubbed off” collagen along the inner ring.

(56) TABLE-US-00003 Sir/Sor 1.19

Example 3

(57) R2L-SR is a non edible straight collagen casing commercialised by Viscofan S.A. Pamplona/Spain. It is inline post rounded according to the following inventive example 1.

(58) R2L calibre 39 directly taken from the production dryer is first guided along a casing collector buffer not shown in FIG. 1 for compensating speed deviations.

(59) Casing humidity is enriched while passing the water ring sprayer (5) as described in FIG. 1.

(60) R2L-SR is post rounded as described in inventive example 1.

(61) TABLE-US-00004 Crosslinking chemical + thermal crosslinking Humidity of the casing as it leaves 11.7% balanced to the total weight the dryer After enrichment 18.7% balanced to the total weight Glycerol 14.0% balanced to the total weight Inflation pressure 300 mbar Inflated calibre laser reading 39.3 mm Diameter of the stainless steel 180 mm roller 7 Hot air temperature blown through 85° C. 6 Outside surface temperature of 50° C. roller 7 Post rounding speed 31 m/min. Resulting inner ring diameter 15 195 mm Resulting inflated calibre 17 39.4 mm No collagen is rubbed off. Sir/Sor 1.30

(62) The resulting post rounded casing of this inventive example 3 is directly compared with the casing of the comparative example C:

(63) Clear visual detection of rubbed off collagen along the inner ring.

(64) TABLE-US-00005 Sir/Sor 1.10

(65) The post rounded casing passes a second casing buffer, not shown in FIG. 1, is then further conveyed into the inline shirring machine.

Example 4

(66) A reel of straight thin collagen casing Colfan JF caliber 17, commercialized by Viscofan S.A:/Spain is post rounded by applying the same technique described in the inventive example 1. Resulting casing has a small ring.

(67) TABLE-US-00006 Croslinking not crosslinked Humidity 19.2% balanced to the total weight Glycerol 21% balanced to the total weight Inflation pressure 350 mbar Inflated calibre laser reading 15.0 mm Diameter of the stainless steel 130 mm roller 7 Hot air temperature for post  245° C. rounding blown through 6 Outside surface temperature of 27.5° C. stainless steel roller 7 Post rounding speed 10 m/min.

(68) No collagen is “rubbed off”.

(69) TABLE-US-00007 Sir/Sor 1.30

Application Test

(70) Foodstuff: “Wiener Sausage” (Traditional Recipe)

(71) TABLE-US-00008 22 kg lean pork 18 kg pork fat 12 kg ice 1.040 kg nitrite pickling salt (NPS) 0.052 kg diphosphate 0.520 kg Wiener spice mixture 0.052 kg white pepper 0.026 kg seasoning

(72) Pork, NPS and diphosphate are first chopped at moderate blade rotations. ⅓ of ice is added and chopping continued at increased blade rotations. At 0° C. another ⅓ of ice is added and chopping continued. Last step is repeated once again. At 3° C. emulsion temperature Wiener spice mixture and seasoning are added. At 4° C. pork fat is added and chopping is continued at increased blade rotations up to 12° C. As last step the meat emulsion is degassed at moderate blade rotations for additional 60 seconds.

(73) Casing samples of comparative examples A and B as well as inventive examples 2 and 3 are stuffed with this Wiener emulsion on a Handtmann VF 80 vacuum filler, portioned and linked by the automatic Handtmann PA 30-7 to sausage chains consisting of 80 g sausages each.

(74) All samples resisted the stuffing, portioning and linking without causing interruptions.

(75) They are then hanged two sausages per turn and pasteurised at 76° C. according to standard guidelines. All Wiener resisted this thermal processing without scrap.

(76) An expert panel consisting of 6 persons first checked the appearance of the finished Wiener, the results clearly underline, that the Wiener processed in the post rounded samples of the inventive examples 1 and 2 show a competitive overall appearance and are both superior to SCC of comparative example A and almost as good as natural Sheep Saitling of comparative example B regarding their sensorial properties.