RETRACTABLE GUIDE
20230255254 · 2023-08-17
Inventors
Cpc classification
B29C48/355
PERFORMING OPERATIONS; TRANSPORTING
B29C48/022
PERFORMING OPERATIONS; TRANSPORTING
B29C48/885
PERFORMING OPERATIONS; TRANSPORTING
B29C48/40
PERFORMING OPERATIONS; TRANSPORTING
B29C48/90
PERFORMING OPERATIONS; TRANSPORTING
International classification
B29C48/00
PERFORMING OPERATIONS; TRANSPORTING
B29C48/25
PERFORMING OPERATIONS; TRANSPORTING
B29C48/885
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A retractable guide (200) is provided for use in a cooling die (202) for the manufacture of extruded food products. The retractable guide (200) is configured to be secured between an input end and an output end of the cooling die (202). A method of high moisture extrusion suitable for manufacturing foodstuffs is also provided, which comprises inserting the retractable guide (200) into a cooling die (202).
Claims
1. A retractable guide for use in a cooling die for the manufacture of extruded food products; wherein the retractable guide is configured to be secured between an input end and an output end of the cooling die.
2. The retractable guide of claim 1, wherein the retractable guide has a locked position, in which it is secured between an input end and an output end of the cooling die; and an unlocked position, in which it is retractable from the cooling die.
3. The retractable guide of claim 1, wherein the retractable guide has a first end, a second end and an intermediate portion, and the first end of the retractable guide is configured to be attached to an extrudate end of the cooling die and the second end of the retractable guide is configured to be attached an output end of the cooling die.
4. The retractable guide of claim wherein the first end of the retractable guide is secured to the extrudate end of the cooling die via a first fixing and the second end of the retractable guide is secured to the output end of the cooling die via a second fixing.
5. The retractable guide of claim 1 wherein the retractable guide is the same length as the cooling die.
6. The retractable guide of claim 1 further comprising a flow splitter attached to a first end of the retractable guide.
7. The retractable guide of claim 1 wherein the retractable guide further comprises an integrated cooling channel.
8. The retractable guide of claim 1 wherein the retractable guide has a cross-sectional profile that varies along the length of the retractable guide.
9. The retractable guide of claim 1 wherein the retractable guide has a first cross-sectional profile at a first end of the retractable guide and a second cross-sectional profile at a second end of the retractable guide, wherein the first and second cross-sectional profiles are different.
10. The retractable guide of claim 1 wherein the retractable guide has a surface roughness that varies along the length of the retractable guide.
11. The retractable guide of claim 1 wherein the retractable guide has a first surface roughness at a first end of the retractable guide and a second surface roughness at a second end of the retractable guide, wherein the roughness of the first surface roughness and the second surface roughness are different.
12. A cooling die for use in the manufacture of extruded food products comprising the retractable guide of claim 1.
13. A high moisture extrusion apparatus for use in the manufacture of extruded food products, comprising: a cooling die, wherein the cooling die further comprises a retractable guide for use in the cooling die; wherein the retractable guide is configured to be secured between an input end and an output end of the cooling die.
14. The cooling die of claim 12, comprising more than one retractable guide.
15. A method of high moisture extrusion suitable for manufacturing foodstuffs, comprising the steps of: inserting the retractable guide of claim 1 into a cooling die; outputting a material from an extruder barrel and inserting the material into a cooling die; passing the material through the cooling die; and outputting the material from the cooling die.
16. A foodstuff product obtained by the process of high moisture extrusion of claim 15.
17. The high moisture extrusion apparatus of claim 13, comprising more than one retractable guide.
Description
SUMMARY AND FIGURES
[0008] An invention is set out in the independent claims, and optional features are set out in the dependent claims.
[0009] The present invention will now be described, by way of example only, with reference to the accompanying drawings.
[0010]
[0011]
[0012]
[0013]
[0014]
[0015]
[0016]
[0017]
[0018]
[0019]
[0020]
[0021]
[0022]
[0023]
[0024]
DETAILED DESCRIPTION
[0025] The present disclosure will now be described by way of example only. These are not the only ways that the disclosure may be put into practise.
[0026] By way of background, as is well known, extrusion is a continuous mixing, kneading, and shaping process used to produce a desired product. Food extrusion is not new to the food industry and has been utilized to produce many different types of food products for more than 60 years. Well known extrusion applications in the food industry include pasta, breakfast cereals, baby food, pet food, and other confectionery products. Almost all of these applications take place at low to intermediate level moisture contents (for a water weight of less than 40%).
[0027] High moisture extrusion is a relatively new type of extrusion. High moisture extrusion cooking describes a process that allows the formation of strands or larger pieces from protein rich powders, slurries or small pieces such as plant proteins, meat and fish. High-moisture extrusion cooking of plant proteins has recently gained increasing attention for producing meat alternatives. The combination of heating and subsequent cooling of the protein—water mixture facilitates the texturization of the product and produces a layered or fibrous structure with a ‘meat like’ appearance. High moisture extrusion is characterised by processing materials with a high water content, compared to traditional extrusion methods. Typically, the materials used in high moisture extrusion have a water weight higher than 40% and often higher than 50%. Due to the unusually high water content in the processed materials and due to the elevated temperature needed to produce the desired effect, the viscosity of the material in the extruder is relatively low (i.e. a creamy, purée like texture). The viscosity and high temperature means that the under typical processing conditions the mixing of materials within the extruder barrel is very effective. Counterintuitively this can adversely affect for example the appearance of conventionally marbled products. Often, high moisture extrusion is therefore combined with a twin screw extruder for making unconventional food products.
[0028] The high moisture extrusion process can be affected by several independent process variables such as raw material characteristics, the high moisture extrusion apparatus and process design on the formation of fibrous structures. Concurrently, the effects of dependent system parameters such as pressure, temperature, and changes at a molecular level with focus on protein—protein interactions can also significantly affect the extruded product. In particular, the process is sensitive to a combination of temperature profile in the extruder, the exposed temperature of the injected products, the selected place of injection, the screw profile of the extruder, quantity and composition of the injected liquid as well as frequency of the injection. These factors are all considered in this application.
Apparatus for High Moisture Extrusion
[0029] Referring to
[0030] The extruder barrel 102 comprises an inlet port 108 and an outlet port 118. The extruder barrel 102 has an inlet end 104 at or near which the inlet port 108 is located and an outlet end 106 at or near which the outlet port 118 is located. The inlet port 108 and the outlet port 118 could be located at opposing ends of the extruder barrel 102 or respectively downstream and upstream thereof. The extruder barrel 102 further comprises an injection port 114.
[0031] The extruder barrel 102 may comprise more than one inlet port 108. For example, the inlet port 108 may comprise a first inlet port, a second inlet port and optionally a third inlet port. The first inlet port may be used to input a dry powder mix (e.g. soy), the second inlet port may be used to input water and the third inlet port may be used to input oils into the extruder barrel 102.
[0032] The inlet port 108 is for input of a first material 110. The injection port 114 is for input of a second material 116. The outlet port 118 is for output of a combination of the first material 110 and the second material 116 from the extruder barrel 102. The injection port 114 is located intermediate to the inlet port 108 and the outlet port 118. The injection port 114 may be located closer to the outlet port 118 than the inlet port 108. The injection port 114 could be located adjacent to the outlet port 118. The outlet port 118 and injection port 114 could both be located at the outlet end 106 of the barrel.
[0033] The first material 110 could comprise protein rich powders, slurries or small pieces such as plant protein or meat and fish. The first material 110 will also comprise a high level of water. The first material 110 has a first weight and typically more than 40% of the total first weight will be water. The water content is needed to ensure the high moisture extrusion process can occur effectively in the extruder barrel 102. The second material 116 could comprise a colourant or flavouring or other nutrients (e.g. vitamins) or combination of colourants, flavourings or nutrients. For example, the second material could comprise organic colouring ingredients, such as plant extracts from red beetroot, saffron, paprika, red radish and/or black carrot. In conventional arrangements, these ingredients do not withstand the high temperatures present in the extruder barrel 102 and fade or turn to unwanted brownish or dark colours. Additionally, the second material 116 may also comprise heat sensitive flavouring compounds, spices and/or vitamins.
[0034] As shown in
Cooling Die Assembly
[0035] A cooling die assembly 122, in accordance with the invention, for use at the delivery end of a high moisture proteinaceous food extruder, is shown in
[0036]
[0037] As shown in
[0038]
[0039] The retractable guide 200 shown in the figures is rectangular in shape, however the retractable guide 200 can also feasibly be any possible shape that fits within the cavity of the cooling die 202. The retractable guide has a first end 211, a second end 212 and an intermediate portion 213 (see
[0040] The retractable guide 200 shown in
[0041] The retractable guide 200 has a locked position, in which it is secured between an input end and an output end of the cooling die; and an unlocked position, in which it is retractable from the cooling die. The locked and unlocked position can be achieved though a variety of different locking mechanisms, some examples of which are described.
[0042] The first end 211 of the retractable guide 200 is attached to the extrudate end 206 of the cooling die 202. This attachment can be via a first fixing. The second end 212 of the retractable guide 200 is attached to the output end 208 of the cooling die 202. This can be via a second fixing. The first and second fixing may correspond to the protruding end portions 214. The first and second fixings can be located externally to the cavity of the cooling die, for example on the extrudate end 206 and on the output end 208. They can also be located on the outer surface of the cooling die. Alternatively, the first and second fixings can be located internally within the cavity of the cooling die (not shown).
General Description of Fixing Mechanisms
[0043] Using the first and second fixings, the retractable guide 200 is held securely in position within the cavity of the cooling die 202. The first and second fixings can be held in either a locked position, when the retractable guide is fixed to the cooling die 202, or an unlocked position, when the retractable guide 200 is free to be removed from the cooling die. The retractable guide 200 can be removed from the cooling die 202 by setting the first and second fixings to the unlocked positions and sliding the retractable guide 200 down the length of the cavity of the cooling die 202. Similarly, the retractable guide 200 may be inserted into the cooling die 202 by pushing the retractable guide down the length of the cavity of the cooling die 202, positioning the first and second fixings and setting the first and second fixings to the locked position. The retractable guide 200 is reusable can be continually removed and inserted into the cooling die 202. In this way, it is possible to reconfigure the cooling die 202 quickly and easily as the retractable guide 200 can be removed and inserted quickly and efficiently. The retractable guide 200 can also be replaced with different types of retractable guides (e.g. different shape, texture) to create a cooling die channel with different characteristics.
[0044] The retractable guide 200 must fit within the cavity of the cooling die 202 between the surface of the cooling die 202 and the inner portion 204. The retractable guide 200 can be added or removed from the cooling die 202 with minimal tools, in a short space of time. The retractable guide 200 produces shear edge effects on the extrudate product as it passes through the cooling die 202. A frictional force between the surface of the retractable guide 200 and the extruded product causes a more fibrous product to be output from the cooling die 202.
[0045]
[0046] An exploded view of the fixing 700 is shown in
[0047] Instead of both ends of the guides having the same fixing as shown in
[0048] The configurations shown in
[0049]
[0050] The primary fixing 802 comprises a fixing element 822 that is secured to the retractable guide via a welded joint 820, as shown in
[0051]
[0052] The fixing plate 806 shown in
[0053] The retractable guide 200 is inserted into the cooling die 202 at the extruder end 206(as shown by the arrow A in
[0054] The secondary fixing 804 can be assembled, disassembled and reassembled again to move between the locked and unlocked positions, thereby allowing the retractable guide 200 to be inserted and removed from the cooling die 202.
Multiple Flow Guides
[0055]
[0056] Multiple retractable guides 200 can be used to vary the output of the extruded product. In particular, by increasing the amount of extruded product that comes into contact with a retractable guide there is an increased frictional resistance and therefore the output product can be produced with a more fibrous structure. The fibrous structure can also be delivered to a greater volume of extruded product within a smaller timeframe. The multiple flow guides can also be used to split the flow into different ‘slabs’ of extruded product. The greater the number of retractable guides the greater the number of ‘slabs’ that may be produced.
[0057] Multiple retractable guides 200 can be distributed radially around the cylindrical die at equal spacings or laterally across a cooling die with a rectangular cross section. Similarly, the spacing of retractable guides 200 can be modified depending on the desired parabolic flow speed profile of the extruded product (see
Flow Splitter
[0058] As an optional feature a flow splitter 900 can be applied to the first end 211 of the retractable guide (i.e. where the extruder barrel connects to the cooling die). An example of a flow splitter 900 is shown in
[0059] The purpose of the flow splitter 900 is to reduce the friction and pressure as the extruded product flows from the extruder barrel to the cooling die 202. This therefore reduces the pressure at the connection point between the extruder barrel and the cooling die 202 and allows for a smooth transition of the extruded product. This also reduces blockages and leakages of extruded product at the connection point. Therefore, the flow splitter 900 mitigates any disadvantages of using the retractable guide 200 (such as interruption of flow caused at the connection point of the extruder barrel and cooling die 202).
[0060] The sharp point 902 is designed to minimise the pressure on the retractable guide and facilitate transfer of extruded product.
Integrated Cooling
[0061] The retractable guide 200 may also include an integrated cooling system as shown in
[0062]
[0063]
Advantages of the Invention
[0064] The retractable flow guide 200 creates a simple but effective way to be able to guide the flow of material through a cooling die 202, without needing to fundamentally or permanently alter the cooling die itself. This has the advantage that it can be applied to cooling die if required and then removed if no longer desirable. The changing of the properties of the cooling die can therefore be optimised to produce peak performance. The changing of the properties of the cooling die can also be conducted in a much shorter time span than it would take to weld various channels for instance. Instead, the intent with the removable guide is that it can be added or removed with minimal tools, in a short space of time, reducing production down time and increasing the variety of products a single cooling die can produce.
[0065] The retractable guide 200 produces shear edge effects on the extrudate product as it passes through the cooling die 202. A frictional force between the surface of the retractable guide 200 and the extruded product causes a more fibrous product to be output from the cooling die 202.
[0066] Speed profiles of the extruded product are shown in
[0067] In
[0068] The zone highlighted by the ‘spotted texture’ in
[0069] The retractable guide 200 is inserted at the position where the flow unexpectedly slows down. Therefore. this maximizes the shear forces experienced at this position. This position is chosen as it leads to better fibre formation throughout the extruded product.
[0070] This leads to the production of a foodstuff product that is more fibrous in texture and therefore allows the composition of meat and fish to be created in a meat alternative product. The end result is a more ‘meat-like’ food product.
[0071] The flow guide does not need to be the full width of the channel, and different material properties can be obtained by varying the proportion of the channel is blocked off. Similarly, different segments of the removable guide may be made from different thicknesses.
[0072] The retractable guide 200 can have a cross-sectional profile that varies along the length of the retractable guide 200. This can be useful to vary the amount of surface friction received by the extrudate product at different positions in the cooling die 202. The retractable guide 200 can have a first cross-sectional profile at a first end 211 of the retractable guide 200 and a second cross-sectional profile at a second end 212 of the retractable guide 200 and the first and second cross-sectional profiles can be different. Alternatively, modelling techniques may be used to understand the most desirable cross-sectional profile of the cooling die and these profiles can be applied to the retractable guide 200. For example, the retractable guide 200 may have a square shaped cross sectional profile at the first end 211 and a triangular shaped cross-sectional profile at the second end 212. Other possible shaped cross-sectional profiles will also be considered depending on the shape of the cooling die and desired output characteristics of the extruded product.
[0073] Similarly, the same techniques can be applied to surface roughness and texture to vary the amount of frictional force imparted to the extruded product at different positions in the cooling die 202. The retractable guide 200 can have a surface roughness that varies along the length of the retractable guide 200. The retractable guide 200 has first surface roughness at a first end 211 of the retractable guide and a second surface roughness at a second end 212 of the retractable guide 200, and the first and second surface roughness's can be different.
[0074] The material could be flexible to encourage a radial flow, the surface roughness can be adapted to increase or decrease the fibre formation resulting from shear effects on the flow or multiple guides could be used to significantly increase the shear effect imparted onto the product flow.