DK177178B1 - Optimized surface for freezing cylinder - Google Patents

Optimized surface for freezing cylinder Download PDF

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Publication number
DK177178B1
DK177178B1 DKPA201170004A DKPA201170004A DK177178B1 DK 177178 B1 DK177178 B1 DK 177178B1 DK PA201170004 A DKPA201170004 A DK PA201170004A DK PA201170004 A DKPA201170004 A DK PA201170004A DK 177178 B1 DK177178 B1 DK 177178B1
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DK
Denmark
Prior art keywords
flow
grooves
cylinder according
freezing cylinder
freezing
Prior art date
Application number
DKPA201170004A
Other languages
Danish (da)
Inventor
Carsten Hermansen
Original Assignee
Tetra Laval Holdings & Finance
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tetra Laval Holdings & Finance filed Critical Tetra Laval Holdings & Finance
Priority to DKPA201170004A priority Critical patent/DK177178B1/en
Priority to BR112013016867A priority patent/BR112013016867A2/en
Priority to CN201180064267.1A priority patent/CN103327825B/en
Priority to MX2013007788A priority patent/MX2013007788A/en
Priority to PCT/DK2011/050515 priority patent/WO2012092929A1/en
Priority to EP11808570.3A priority patent/EP2661177A1/en
Priority to US13/978,410 priority patent/US20130319645A1/en
Priority to RU2013136395/13A priority patent/RU2592570C2/en
Application granted granted Critical
Publication of DK177178B1 publication Critical patent/DK177178B1/en

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/10Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
    • F28D7/106Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically consisting of two coaxial conduits or modules of two coaxial conduits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23GCOCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
    • A23G9/00Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor
    • A23G9/04Production of frozen sweets, e.g. ice-cream
    • A23G9/14Continuous production
    • A23G9/16Continuous production the products being within a cooled chamber, e.g. drum
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23GCOCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
    • A23G9/00Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor
    • A23G9/04Production of frozen sweets, e.g. ice-cream
    • A23G9/22Details, component parts or accessories of apparatus insofar as not peculiar to a single one of the preceding groups
    • A23G9/222Freezing drums
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/105Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being corrugated elements extending around the tubular elements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/126Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element consisting of zig-zag shaped fins
    • F28F1/128Fins with openings, e.g. louvered fins
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/24Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
    • F28F1/26Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means being integral with the element
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B39/00Evaporators; Condensers
    • F25B39/02Evaporators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25CPRODUCING, WORKING OR HANDLING ICE
    • F25C1/00Producing ice
    • F25C1/12Producing ice by freezing water on cooled surfaces, e.g. to form slabs
    • F25C1/14Producing ice by freezing water on cooled surfaces, e.g. to form slabs to form thin sheets which are removed by scraping or wedging, e.g. in the form of flakes
    • F25C1/145Producing ice by freezing water on cooled surfaces, e.g. to form slabs to form thin sheets which are removed by scraping or wedging, e.g. in the form of flakes from the inner walls of cooled bodies
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0042Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for foodstuffs
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/08Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
    • F28F21/081Heat exchange elements made from metals or metal alloys
    • F28F21/082Heat exchange elements made from metals or metal alloys from steel or ferrous alloys
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/08Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
    • F28F21/081Heat exchange elements made from metals or metal alloys
    • F28F21/085Heat exchange elements made from metals or metal alloys from copper or copper alloys
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/08Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
    • F28F21/081Heat exchange elements made from metals or metal alloys
    • F28F21/087Heat exchange elements made from metals or metal alloys from nickel or nickel alloys

Abstract

A freezing cylinder is disclosed cornprising on its outer surface a set of substantially parallel longitudinal cooling fins and a set of substantially parallel grooves intersecting the set of cooling fins, preferably at a right angle.A freezing cylinder is disclosed cornprising on its outer surface a set of substantially parallel longitudinal cooling fins and a set of substantially parallel grooves intersecting the set of cooling fins, preferably at a right angle.

Description

DK 177178 B1
Optimised surface for freezing cylinder Field of the invention 5 The present invention relates to a freezing cylinder for use, for instance, in an apparatus for the production of frozen ice cream.
Background of the invention 10 In the production of edible ice cream products, it is well-known to use so-called through-flow freezers. Often, such freezers comprise a freezing cylinder through which the ice cream mass is transported, typically by pumping or by means of a conveyor screw. The freezing cylinder is being cooled from its outside using a liquid coolant such as, for instance, ammonia (NH3), carbon dioxide (CO2) or some sort of 15 Freon, such as R404a. During the freezing process, the coolant absorbs heat energy from the outer cylinder surface mainly due to a phase-shift from liquid to gaseous phase of the coolant, whereby tiny gas bubbles containing evaporated coolant are formed on the outer cylinder surface.
20 The cooling efficiency of such a system depends on a number of factors. One important factor is the area of the cylinder surface to be cooled, which can be increased by well-known means, such as the use of cooling fins extending from the surface. However, also other factors affecting the evaporation rate, the size of the bubbles and the rate at which the bubbles leave the cylinder surface through the still 25 liquid coolant are important for the efficiency of the cooling system. This is due to the fact that bubbles staying at the cylinder surface form an insulating layer between the cylinder surface and the liquid coolant, thus reducing the transportation of heat energy from the cylinder surface to the liquid coolant. The relation is relatively straightforward: The more the bubbles adhere to the surface of the freezing cylinder, 30 the more the surface is covered with insulating air bubbles, and the more the heat transfer coefficient is reduced. These properties relating to the formation and the 2 DK 177178 B1 removal of the gas bubbles depend mainly on the properties of the liquid coolant and on the structure of the cylinder surface.
The surface structure may be improved for a better cooling efficiency by means of 5 so-called nano coating. However, this is a very expensive way of obtaining a better cooling efficiency.
EP 0670461 A1 discloses a freezing drum, in which a cylindrical freezing chamber is coaxially positioned inside a cylindrical external jacket, wherein a spiral-shaped path 10 is provided in the hollow space between the jacket and the chamber, through which path a thermal exchange fluid circulates from an inlet to an outlet.
It is an object of the present invention to provide a more cost-efficient way of optimising the surface of a freezing cylinder for obtaining a significantly better 15 cooling efficiency of a through-flow freezer comprising such a freezing cylinder.
Brief description of the invention
The present invention relates to a through-flow freezing cylinder comprising on its 20 outer surface a set of substantially parallel tangential cooling fins and a set of substantially parallel grooves intersecting the set of cooling fins.
Contrary to the disclosure of EP 0670461 A1 as described above, the use of the present invention does not involve a thermal exchange fluid circulating along a 25 predefined path in a hollow space between a freezing chamber and an external jacket.
Rather, a thermal exchange fluid in the form of a liquid coolant must simply be placed to be in contact with the outer surface of the freezing cylinder as described further below.
3 DK 177178 B1
This means that there are no requirements relating to the shape of an external jacket, in which the freezing cylinder may be placed or to the positioning of the freezing cylinder in relation to such a jacket.
5 It has surprisingly been found that by structuring the outer surface of the freezing cylinder with a set of parallel grooves intersecting a set of parallel cooling fins, the freezing efficiency of a through-flow freezer comprising the freezing cylinder can be increased by up to about 20 % without increasing the size of the freezer.
10 In an embodiment of the invention, the grooves intersect the cooling fins at an angle of more than 30°, preferably at an angle of more than 60°, most preferably at a substantially right angle.
It has been found that the best results are obtained if the angle of intersection 15 between the grooves and the cooling fins is not very acute.
In a preferred embodiment of the invention, the cooling fins and the grooves are oriented tangentially and axially, respectively, in relation to the freezing cylinder.
20 For production purposes, this configuration of the cooling fins and the grooves requires a relatively simple set-up of tools, for instance for machining the grooves.
In an embodiment of the invention, the cooling fins have a substantially triangular cross-sectional shape.
25
In an embodiment of the invention, the maximum height of the cooling fins is between 0.5 mm and 10 mm, preferably between 1 mm and 5 mm, most preferably between 2.5 mm and 3.5 mm.
i DK 177178 B1 4
In an embodiment of the invention, the mutual distance between the centrelines of two neighbouring cooling fins is between 0.5 mm and 10 mm, preferably between 1 mm and 5 mm, most preferably between 2.5 mm and 3.5 mm.
5 In an embodiment of the invention, the maximum width of the cooling fins is between 0.5 mm and 10 mm, preferably between 1 mm and 5 mm, most preferably between 2.5 mm and 3.5 mm.
In an embodiment of the invention, the mutual distance and the maximum width of 10 the cooling fins are substantially the same.
In an embodiment of the invention, the grooves have a substantially rectangular cross-sectional shape.
15 In an embodiment of the invention, the mutual distance between two neighbouring grooves is between 1 mm and 12 mm, preferably between 2 mm and 10 mm, most preferably between 5 mm and 7 mm.
In an embodiment of the invention, the maximum width of the grooves is between 20 0.2 mm and 4 mm, preferably between 0.5 mm and 2 mm, most preferably between 0.8 mm and 1.2 mm.
In an embodiment of the invention, the maximum depth of the grooves is between 0.2 mm and 6 mm, preferably between 0.5 mm and 6 mm, most preferably between 25 2 mm and 3 mm.
It has been shown that the optimum freezing efficiency is obtained by choosing the properties of the cooling fins and the grooves within the above-specified ranges.
30 In an embodiment of the invention, the grooves are machined.
DK 177178 B1 5 i |
Machining the grooves (and often also the cooling fins) rather than casting a complete freezing cylinder with cooling fins and intersecting grooves is advantageous in that it results in a relatively rough surface containing numerous tiny burrs, which have shown also to contribute to the optimisation of the cooling 5 efficiency of the system.
In preferred embodiments of the invention, the through-flow freezing cylinder is made from nickel, brass, stainless steel or black steel.
10 Making the freezing cylinder from nickel is advantageous in that nickel has high specific heat conductivity.
If brass is in contact with ammonia, which is one of the preferred cooling media in through-flow freezers of the type comprising freezing cylinders like the one of the 15 present invention, the ammonia will react with the copper in the brass alloy, which can destroy the structure made from the brass. However, if another cooling media, such as carbon dioxide or Freon, is to be used, the freezing cylinder may advantageously be made from brass, which is substantially less expensive than nickel. Like nickel, brass has high specific heat conductivity.
20
The freezing cylinder may also be made from stainless steel, which is less expensive than nickel and brass. However, the use of stainless steel results in a lower freezing capacity due to the relatively poor heat transfer capabilities of this material.
25 Due to the low price of black steel, it is also considered to make the freezing cylinder from this material. This, however, requires a coating of the inner side of the cylinder wall for hygienic reasons.
In some embodiments of the invention, the freezing cylinder will be coated on the 30 inner side of its wall with a layer of hard chrome or the like in order to make it more wear-resistant.
6 DK 177178 B1
Figures A few exemplary embodiments of the invention will be described in the following 5 with reference to the figures, of which fig. 1 illustrates schematically a cross-section of a through-flow freezer comprising a freezing cylinder according to an embodiment of the invention and 10 fig. 2 illustrates schematically the structure of an outer surface of a freezing cylinder according to an embodiment of the invention.
Detailed description of the invention 15
Fig. 1 illustrates schematically a cross-section of a through-flow freezer 1 in which a freezing cylinder 3 according to an embodiment of the invention is placed inside an outer cylinder 2. The distance between the walls of the two cylinders 2, 3, respectively, will often be relatively small, such as between 10 mm and 40 mm.
20 , The outer surface of the freezing cylinder 3 is provided with a number of tangentially oriented cooling fins 4, which are intersected by a number of longitudinally oriented grooves 5. The mass 6 to be frozen, for instance edible ice cream mass 6, is transported through the freezing cylinder 3. Inside the freezing cylinder 3, one or 25 more scrapers (not shown) scrape the layer of frozen ice cream mass 6 continuously formed on the inner surface of the freezing cylinder 3 off the cylinder wall.
i A liquid coolant 7 is placed in the cavity between the inner surface of the outer cylinder 2 and the outer surface of the freezing cylinder 3 for cooling the freezing 30 cylinder 3 and its contents 6 by absorbing heat energy from the freezing cylinder 3, mainly due to a phase-shift from liquid to gas phase of some of the coolant 7.
7 DK 177178 B1
The freezing cylinder 3 is typically made from nickel, brass, stainless steel or black steel depending on the type of coolant 7 with which it is meant to be used.
5 Brass is an alloy of copper and zinc. Ammonia reacts with copper resulting in the formation of cracks in brass structures in contact with ammonia. Eventually, such structures may collapse. Therefore, the use of ammonia as coolant 7 generally requires that the freezing cylinder 3 is made from nickel or steel. Brass, which is less expensive than nickel and still has high specific heat conductivity, can be used if 10 another coolant 7 than ammonia such as, for instance, carbon dioxide or Freon is to be used. Generally, the cooling effect obtainable with carbon dioxide is about 25 % higher than the one obtainable with ammonia. However, the pressure required is also higher for carbon dioxide than for ammonia.
15 The structure of the outer surface of the freezing cylinder 3 is important for the adhesion of the gas bubbles to the freezing cylinder 3 surface and, thus, for the cooling efficiency of the through-flow freezer 1. Fig. 2 illustrates schematically the structure of an outer surface of a freezing cylinder 3 according to an embodiment of the invention in which a plurality of parallel and tangentially oriented cooling fins 4 20 are intersected by a number of parallel and longitudinally oriented grooves 5.
Numerous investigations have revealed that the cooling efficiency can be optimized by choosing the height of the cooling fins 4 to be about 3 mm, the width and depth of the intersecting grooves 5 to be approximately 1 mm and 2.5 mm, respectively, and 25 the mutual distance between two neighbouring grooves 5 to be between 5 mm and 7 mm.
Optimisation investigations relating to the height of the cooling fins 4 alone, i.e. without using any intersecting grooves 5, have shown to result in an increase of the 30 cooling efficiency and, thus, of the freezer capacity of up to about 5 % without increasing the size of the freezer 1.
8 DK 177178 B1
However, the addition and optimisation of intersecting grooves 5 surprisingly turned out to lead to more significant increases of the cooling efficiency, namely up to about 20 % as compared to through-flow freezers known from the art using freezing 5 cylinders having cooling fins of a height of approximately 1.5 mm.
The investigations have shown that similar increases in evaporation and, thus, in cooling efficiency are obtained, whether the coolant 7 used is ammonia, carbon dioxide or nitrogen, and whether the freezing cylinder 3 is made from nickel, brass or 10 stainless steel.
9 DK 177178 B1
List of reference numbers | 1. Through-flow freezer 2. Outer cylinder 5 3. Freezing cylinder 4. Cooling fin 5. Groove 6. Mass to be frozen 7. Liquid coolant 10

Claims (14)

1. Gennemstrømningsfrysecylinder (3), som på sin udvendige overflade omfatter et sæt i det væsentlige parallelle tangentielle kølefinner (4) og et sæt i det væsentlige parallelle riller (5), der krydser sættet af 5 kølefinner.A flow-freeze cylinder (3) comprising on its outer surface a set of substantially parallel tangential heat sinks (4) and a set of substantially parallel grooves (5) intersecting the set of 5 heat sink fins. 2. Gennemstrømningsfrysecylinder ifølge krav 1, hvor rillerne krydser kølefinneme i en vinkel på mere end 30°, fortrinsvis i en vinkel på mere end 60°, mest foretrukket i en i det væsentlige ret vinkel.A flow freezing cylinder according to claim 1, wherein the grooves cross the cooling fins at an angle of more than 30 °, preferably at an angle of more than 60 °, most preferably at a substantially right angle. 3. Gennemstrømningsfrysecylinder ifølge krav 1 eller krav 2, hvor kølefinneme 10 og rillerne er orienteret henholdsvis tangentielt og aksialt i forhold til frysecylinderen.Flow freezing cylinder according to claim 1 or claim 2, wherein the cooling fins 10 and the grooves are respectively tangentially and axially oriented with respect to the freezing cylinder. 4. Gennemstrømningsfrysecylinder ifølge et hvilket som helst af de foregående krav, hvor kølefinneme har en udformning, der i det væsentlige har et trekantet tværsnit.Flow freezing cylinder according to any one of the preceding claims, wherein the cooling fins have a configuration having substantially a triangular cross-section. 5. Gennemstrømningsfrysecylinder ifølge et hvilket som helst af de foregående krav, hvor kølefinnemes maksimale højde er mellem 0,5 mm og 10 mm, fortrinsvis mellem 1 mm og 5 mm, mest foretrukket mellem 2,5 mm og 3,5 mm.Flow freeze cylinder according to any one of the preceding claims, wherein the maximum height of the cooling fin is between 0.5 mm and 10 mm, preferably between 1 mm and 5 mm, most preferably between 2.5 mm and 3.5 mm. 6. Gennemstrømningsfrysecylinder ifølge et hvilket som helst af de foregående 20 krav, hvor den indbyrdes afstand mellem midterlinjeme af to nabostillede kølefinner er mellem 0,5 mm og 10 mm, fortrinsvis mellem 1 mm og 5 mm, mest foretrukket mellem 2,5 mm og 3,5 mm.A flow freezing cylinder according to any one of the preceding claims, wherein the distance between the center lines of two adjacent cooling fins is between 0.5 mm and 10 mm, preferably between 1 mm and 5 mm, most preferably between 2.5 mm and 3.5 mm. 7. Gennemstrømningsfrysecylinder ifølge et hvilket som helst af de foregående krav, hvor kølefinnemes maksimale bredde er mellem 0,5 mm og 10 mm, 25 fortrinsvis mellem 1 mm og 5 mm, mest foretrukket mellem 2,5 mm og 3,5 mm. 2 ! DK 177178 B1A flow freezing cylinder according to any one of the preceding claims, wherein the maximum width of the cooling fin is between 0.5 mm and 10 mm, preferably between 1 mm and 5 mm, most preferably between 2.5 mm and 3.5 mm. 2! DK 177178 B1 8. Gennemstrømningsfrysecylinder ifølge et hvilket som helst af de foregående | krav, hvor kølefinnemes indbyrdes afstand og maksimale bredde i det væsentlige er den samme. iFlow freeze cylinder according to any of the preceding | claims in which the spacing and maximum width of the cooling fins are substantially the same. in 9. Gennemstrømningsfrysecylinder ifølge et hvilket som helst af de foregående i 5 krav, hvor rillerne har en udformning, der i det væsentlige har et rektangulært tværsnit. jFlow freeze cylinder according to any one of the preceding claims, wherein the grooves have a configuration having substantially a rectangular cross-section. j 10. Gennemstrømningsfrysecylinder ifølge et hvilket som helst af de foregående j krav, hvor den indbyrdes afstand mellem to nabostillede riller er mellem 1 mm j og 12 mm, fortrinsvis mellem 2 mm og 10 mm, mest foretrukket mellem 5 mm j 10 og 7 mm.A flow freeze cylinder according to any one of the preceding claims, wherein the distance between two adjacent grooves is between 1 mm j and 12 mm, preferably between 2 mm and 10 mm, most preferably between 5 mm j 10 and 7 mm. 11. Gennemstrømningsfrysecylinder ifølge et hvilket som helst af de foregående krav, hvor rillemes maksimale bredde er mellem 0,2 mm og 4 mm, fortrinsvis mellem 0,5 mm og 2 mm, mest foretrukket mellem 0,8 mm og 1,2 mm.A flow freeze cylinder according to any one of the preceding claims, wherein the maximum width of the grooves is between 0.2 mm and 4 mm, preferably between 0.5 mm and 2 mm, most preferably between 0.8 mm and 1.2 mm. 12. Gennemstrømningsfrysecylinder ifølge et hvilket som helst af de foregående 15 krav, hvor rillemes maksimale dybde er mellem 0,2 mm og 6 mm, fortrinsvis mellem 0,5 mm og 6 mm, mest foretrukket mellem 2 mm og 3 mm.A flow freeze cylinder according to any one of the preceding claims, wherein the maximum depth of the grooves is between 0.2 mm and 6 mm, preferably between 0.5 mm and 6 mm, most preferably between 2 mm and 3 mm. 13. Gennemstrømningsfrysecylinder ifølge et hvilket som helst af de foregående krav, hvor rillerne er maskinbearbejdet.A flow freezing cylinder according to any one of the preceding claims, wherein the grooves are machined. 14. Gennemstrømningsfrysecylinder ifølge et hvilket som helst af de foregående 20 krav, hvilken gennemstrømningsfrysecylinder er fremstillet af nikkel, messing, rustfrit stål eller sort stål. i i i j iFlow freezing cylinder according to any one of the preceding claims, which flow freezing cylinder is made of nickel, brass, stainless steel or black steel. i i i j i
DKPA201170004A 2011-01-06 2011-01-06 Optimized surface for freezing cylinder DK177178B1 (en)

Priority Applications (8)

Application Number Priority Date Filing Date Title
DKPA201170004A DK177178B1 (en) 2011-01-06 2011-01-06 Optimized surface for freezing cylinder
BR112013016867A BR112013016867A2 (en) 2011-01-06 2011-12-22 bypass freezing cylinder
CN201180064267.1A CN103327825B (en) 2011-01-06 2011-12-22 For the surface of the optimization of freezing jar
MX2013007788A MX2013007788A (en) 2011-01-06 2011-12-22 Optimised surface for freezing cylinder.
PCT/DK2011/050515 WO2012092929A1 (en) 2011-01-06 2011-12-22 Optimised surface for freezing cylinder
EP11808570.3A EP2661177A1 (en) 2011-01-06 2011-12-22 Optimised surface for freezing cylinder
US13/978,410 US20130319645A1 (en) 2011-01-06 2011-12-22 Optimised surface for freezing cylinder
RU2013136395/13A RU2592570C2 (en) 2011-01-06 2011-12-22 Optimised surface for freezing cylinder

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DKPA201170004A DK177178B1 (en) 2011-01-06 2011-01-06 Optimized surface for freezing cylinder
DK201170004 2011-01-06

Publications (1)

Publication Number Publication Date
DK177178B1 true DK177178B1 (en) 2012-05-07

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BR (1) BR112013016867A2 (en)
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MX (1) MX2013007788A (en)
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WO (1) WO2012092929A1 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR3010176B1 (en) * 2013-08-30 2018-06-29 Gea Refrigeration France ICE GENERATING DEVICE, IMPLEMENTING A DOUBLE-WALL CYLINDRICAL EXCHANGER, INCLUDING A BI-MATERIAL INTERNAL WALL
IT201800006520A1 (en) * 2018-06-20 2019-12-20 HEAT EXCHANGER.

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3062021A (en) * 1960-12-12 1962-11-06 Ansel B Grose Device for dispensing frozen fluffy cream and the like
US3326283A (en) * 1965-03-29 1967-06-20 Trane Co Heat transfer surface
DE2359710A1 (en) * 1973-02-07 1974-08-08 Egidio Prizzon Continuous ice-cream prodn. appts - with pre-mixing element for the liq. starting material which is continuously fed in measured amts. to a cooled, mixing chamber
SU485297A1 (en) * 1974-03-01 1975-09-25 Центральный Научно-Исследовательский Котлотурбинный Институт Им.И.И. Ползунова Heat exchanger tube
US3893322A (en) * 1974-08-21 1975-07-08 Universal Oil Prod Co Method for providing improved nucleate boiling surfaces
US4330036A (en) * 1980-08-21 1982-05-18 Kobe Steel, Ltd. Construction of a heat transfer wall and heat transfer pipe and method of producing heat transfer pipe
US4402359A (en) * 1980-09-15 1983-09-06 Noranda Mines Limited Heat transfer device having an augmented wall surface
US5203404A (en) * 1992-03-02 1993-04-20 Carrier Corporation Heat exchanger tube
DE59403306D1 (en) * 1994-02-26 1997-08-14 Heidenhain Gmbh Dr Johannes Interferometer
IT1273366B (en) 1994-03-04 1997-07-08 G R B S N C Di Grotti Renzo & FREEZING CYLINDER WITH BUILT-IN EVAPORATOR AND METHOD FOR ITS MANUFACTURE
JP3415013B2 (en) * 1997-12-22 2003-06-09 株式会社神戸製鋼所 Heat transfer tube for condenser
US6253573B1 (en) * 1999-03-10 2001-07-03 Specialty Equipment Companies, Inc. High efficiency refrigeration system
GB9917652D0 (en) * 1999-07-28 1999-09-29 Brunnar H F Liquid ice generator
ITBO20050706A1 (en) * 2005-11-22 2007-05-23 Ali Spa METHOD FOR MANUFACTURING A FREEZING CHAMBER AND FREEZING CHAMBER SO IT HAS OBTAINED
RU2305949C1 (en) * 2005-12-16 2007-09-20 Федеральное государственное унитарное предприятие УРАЛЬСКИЙ ЭЛЕКТРОХИМИЧЕСКИЙ КОМБИНАТ Freezing cylinder for ice-cream making machine
JP2009162395A (en) * 2007-12-28 2009-07-23 Showa Denko Kk Double-wall-tube heat exchanger

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MX2013007788A (en) 2013-08-21
EP2661177A1 (en) 2013-11-13
CN103327825B (en) 2016-06-15
RU2013136395A (en) 2015-02-20
BR112013016867A2 (en) 2016-10-11
CN103327825A (en) 2013-09-25
US20130319645A1 (en) 2013-12-05
RU2592570C2 (en) 2016-07-27
WO2012092929A1 (en) 2012-07-12

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