WO2008060218A1 - Adjustable steam injector - Google Patents

Adjustable steam injector Download PDF

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Publication number
WO2008060218A1
WO2008060218A1 PCT/SE2007/000995 SE2007000995W WO2008060218A1 WO 2008060218 A1 WO2008060218 A1 WO 2008060218A1 SE 2007000995 W SE2007000995 W SE 2007000995W WO 2008060218 A1 WO2008060218 A1 WO 2008060218A1
Authority
WO
WIPO (PCT)
Prior art keywords
injector
grooves
product
steam
centre pin
Prior art date
Application number
PCT/SE2007/000995
Other languages
French (fr)
Inventor
Roland Ringström
Original Assignee
Tetra Laval Holdings & Finance Sa
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 Sa filed Critical Tetra Laval Holdings & Finance Sa
Publication of WO2008060218A1 publication Critical patent/WO2008060218A1/en

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28CHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C3/00Other direct-contact heat-exchange apparatus
    • F28C3/06Other direct-contact heat-exchange apparatus the heat-exchange media being a liquid and a gas or vapour
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23CDAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C3/00Preservation of milk or milk preparations
    • A23C3/02Preservation of milk or milk preparations by heating
    • A23C3/03Preservation of milk or milk preparations by heating the materials being loose unpacked
    • A23C3/033Preservation of milk or milk preparations by heating the materials being loose unpacked and progressively transported through the apparatus
    • A23C3/037Preservation of milk or milk preparations by heating the materials being loose unpacked and progressively transported through the apparatus in direct contact with the heating medium, e.g. steam
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L3/00Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
    • A23L3/16Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by heating loose unpacked materials
    • A23L3/18Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by heating loose unpacked materials while they are progressively transported through the apparatus
    • A23L3/22Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by heating loose unpacked materials while they are progressively transported through the apparatus with transport through tubes
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L3/00Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
    • A23L3/16Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by heating loose unpacked materials
    • A23L3/24Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by heating loose unpacked materials with the materials in spray form
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/314Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
    • B01F25/3142Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit the conduit having a plurality of openings in the axial direction or in the circumferential direction
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F27/00Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus

Definitions

  • the present invention relates to an adjustable steam injector comprising an injector housing with an inlet for a product, an outlet for the product, as well as a steam inlet, the injector further including an injector body displaceable in the injector housing, the injector body having, in its one end, a centre pin around which are disposed concentric gaps for steam and product, respectively.
  • Direct heating of the product by introducing steam into the product realises a rapid and efficient heating.
  • This rapid method entails that it is possible to reduce the treatment time, which in total gives a reduced thermal effect on the product, and a product will be obtained which maintains a high standard of quality, above all in terms of flavour.
  • injectors which all display similar construction, with an inlet for the product to be treated and an outlet for the ready-treated product.
  • the injector further has an inlet for steam under high pressure which, through various arrangements involving gaps or ducts, is caused to converge with the product and warm it to the desired temperature.
  • gaps or ducts it may be suitable for products of different viscosities.
  • Swedish Patent Specification SE 367 121 discloses a so-called annular gap injector, where concentric gaps for steam and product are disposed about a centre pin.
  • Annular gap injectors are known for their operational reliability since fouling of the product is not a serious problem.
  • the annular gap injectors may give a poorer admixture of steam in the product, since there will be a stratification of steam and product in the injector outlet.
  • One object of the present invention is to realise an injector whose design and construction enjoys the advantages of the annular gap injector as regards fouling, but which results in an improved mixing of product and steam, in particular for viscous products.
  • the steam injector of the type described by way of introduction has been given the characterising feature that the centre pin has a number of grooves accommodated in its circumferential surface, the grooves being rotated towards the one end of the centre pin.
  • FIG. 1 shows, partly in section, a side elevation of an injector according to the present invention
  • Fig. 2 shows a part of Fig. 1 with two different adjustment positions, shown in magnification
  • Fig. 3 shows a cross section of a groove
  • Fig. 4 shows a side elevation of the centre pin with the angle of rotation of the grooves
  • Fig. 5 shows a top plan view of the centre pin with the distribution angle of the grooves.
  • Fig. 1 shows a steam injector 1 according to the present invention.
  • the steam injector 1 comprises a closed injector housing 2 of substantially tubular appearance.
  • the injector housing 2 displays an inlet 3 for a product which is to be heat treated in the injector 1, as well as an outlet 4 for the heat treated product.
  • the injector housing 2 also has an inlet 5 for steam.
  • the injector housing 2 is suitably manufactured from stainless steel so that it is suitable for use together with foods and so that it is easy to wash in an efficient manner.
  • an injector body 6 which is displaceable in the longitudinal direction of the injector housing 2.
  • an injector body 6 which is displaceable in the longitudinal direction of the injector housing 2.
  • some form of regulator device (not shown).
  • the regulator device may be manual or automatic and, by displacing the injector body 6, it is thus possible to adjust the capacity of the injector 1.
  • a centre pin 8 At the other end of the injector body 6, there is placed a centre pin 8.
  • the centre pin 8 and the injector housing 2 are designed so that concentric gaps are formed around the centre pin 8, of which at least one gap 9 is intended for product and at least one gap 10 is intended for steam.
  • both the centre pin 8 and the injector body 6 are suitably manufactured from stainless steel, so that they are suitable for use with foods and so that they are easy to wash in an efficient manner.
  • the centre pin 8 is, according to the invention, formed so that the first part 11 most proximal the injector body 2 is conical in such a manner that the diameter dimension of the centre pin 8 increases in relation to the diameter dimension of the injector body 6. Moreover, on this first part 11 of the centre pin a number of grooves 12 start which are milled in the circumferential surface of the centre pin 8.
  • the second part 13 of the centre pin 8 is straight, and on this part 13 the grooves 12 continue, partly as straight grooves, i.e. they are axially directed. On the other hand, the grooves 12 begin to turn on this part 13.
  • the grooves 12 are turned through 30-40° and preferably 35° in relation to the longitudinal direction of the injector body 2 and the centre pin 8. This turning is shown in Fig.4 as the angle a.
  • the third part 14 of the centre pin 8 is once again conical with reducing diameter from the diameter of the straight, second part 13.
  • the grooves 12 continue with the same turn throughout the entire circumferential surface of the third part 14.
  • the grooves 12 are, in the preferred embodiment, between 5 and 30 in number, preferably 20 in number, uniformly distributed over the centre pin 8.
  • the number of grooves 12 depends upon capacity and the width of the grooves 12.
  • the preferred number of grooves 12 gives a distribution angle of 18°, which is shown in
  • Fig. 5 by means of the angle ⁇ .
  • the number of grooves 12 may be varied and may be more or fewer than 20 in number. Another number of grooves 12 than in the preferred embodiment would naturally give a different distribution angle.
  • the grooves 12 have a width of 0.5-5 mm and a depth of 0.8-3.5 mm.
  • the grooves preferably display a square, or alternatively rectangular cross section, but other types of cross section may also be employed. In the preferred embodiment, the grooves 12 have a square cross section with a width and depth of 3.5 mm.
  • the guide cone 15 is placed in the outlet 4 for the heat-treated product. The purpose of the guide cone 15 is to control the mixing of product and steam out through the outlet 4.
  • the product which enters into the injector 1 through the product inlet 3 may be a relatively viscous product, such as ice-cream mix, high fat content cream, puddings, soups, children's food or the like.
  • the injector 1 may naturally also be employed for less viscous products.
  • the product which passes in through the inlet 3, into the injector housing 2, will, when it passes the first part 11 of the centre pin 8, be throttled in its flow which will assist in urging the product into the grooves 12 which start on this first part 11.
  • the product then follows the centre pin 8 and the gap 9.
  • an acceleration of the product will be obtained at the same time as the product is more formed as jets, rather than as a concentric column which is the case in conventional annular gap injectors.
  • the present invention realises an adjustable steam injector which displays the advantages of conventional annular gap injectors as far as fouling is concerned, which thus affords long operational times.
  • the design of the injector gives an efficient mixing of product and steam so that there will be obtained a reliable and uniform heating of the product in the injector. The heating will be well defined and there will be obtained the desired bacteriological extermination.

Abstract

The present invention relates to an adjustable steam injector (1) of the type which has an injector housing (2) with an inlet (3) for product which is to be heated and an outlet (4) for the heated product. The injector housing (2) also has an inlet (5) for steam. The injector (1) also includes an injector body (6) displaceable in the injector housing (2) and having, in its one end, a centre pin (8). Around the centre pin (8) there are disposed concentric gaps (9, 10) for product and steam, respectively. The centre pin (8) is formed so that it has a number of grooves (12) accommodated on its circumferential surface. The grooves (12) are turned towards the one end of the centre pin (8).

Description

ADJUSTABLE STEAM INJECTOR
TECHNICAL FIELD
The present invention relates to an adjustable steam injector comprising an injector housing with an inlet for a product, an outlet for the product, as well as a steam inlet, the injector further including an injector body displaceable in the injector housing, the injector body having, in its one end, a centre pin around which are disposed concentric gaps for steam and product, respectively.
BACKGROUND ART
As regards the heat treatment of liquid or pumpable foods, use may be made of steam in order, in a rapid and efficient manner, to heat the food product. One of the methods employed for introducing steam directly into the product is to use an injector. Depending upon the temperature to which it is desired to heat the product, it is possible to obtain a pasteurised or an aseptic product, or alternatively a product having an extended shelf-life in cold storage. The commonest practice is to heat the product which, for example, may be dairy produce, juices, viscous liquid food products or the like, to a temperature at which there is obtained a total extermination of harmful microorganisms. This affords a food product which keeps stable on storage at room temperature. No unbroken refrigerated chain for storage is needed, which may be an advantage above all in third world countries.
Direct heating of the product by introducing steam into the product realises a rapid and efficient heating. This rapid method entails that it is possible to reduce the treatment time, which in total gives a reduced thermal effect on the product, and a product will be obtained which maintains a high standard of quality, above all in terms of flavour.
There are available on the market a large number of injectors which all display similar construction, with an inlet for the product to be treated and an outlet for the ready-treated product. The injector further has an inlet for steam under high pressure which, through various arrangements involving gaps or ducts, is caused to converge with the product and warm it to the desired temperature. Depending upon the design and construction of the injector, with gaps or ducts, it may be suitable for products of different viscosities.
Swedish Patent Specification SE 367 121 discloses a so-called annular gap injector, where concentric gaps for steam and product are disposed about a centre pin. Annular gap injectors are known for their operational reliability since fouling of the product is not a serious problem. On the other hand, as regards viscous products, the annular gap injectors may give a poorer admixture of steam in the product, since there will be a stratification of steam and product in the injector outlet.
An injector for viscous products is described in Swedish Patent Specification SE 517 823. This injector displays an inner product pipe surrounded by a thick- walled pipe with a large number of ducts through which steam is fed to the product. However, this injector has proved to be less suitable for products which are particularly prone to fouling, such as ice-cream mix, high fat content cream, puddings, children's food or the like.
OBJECTS OF THE INVENTION
One object of the present invention is to realise an injector whose design and construction enjoys the advantages of the annular gap injector as regards fouling, but which results in an improved mixing of product and steam, in particular for viscous products.
SOLUTION
This and other objects have been attained according to the present invention in that the steam injector of the type described by way of introduction has been given the characterising feature that the centre pin has a number of grooves accommodated in its circumferential surface, the grooves being rotated towards the one end of the centre pin.
Preferred embodiments of the present invention have further been given the characterising features as set forth in the appended subclaims. BRIEF DESCRIPTION OF THE ACCOMPANYING DRAWINGS
One preferred embodiment of the present invention will now be described in greater detail hereinbelow, with reference to the accompanying Drawings. In the accompanying Drawings: Fig. 1 shows, partly in section, a side elevation of an injector according to the present invention;
Fig. 2 shows a part of Fig. 1 with two different adjustment positions, shown in magnification;
Fig. 3 shows a cross section of a groove; Fig. 4 shows a side elevation of the centre pin with the angle of rotation of the grooves; and
Fig. 5 shows a top plan view of the centre pin with the distribution angle of the grooves.
The Drawings show only those parts essential to an understanding of the present invention, and the positioning of the injector in a heat treatment plant, which is well-known to a person skilled in the art, has been omitted.
DESCRIPTION OF PREFERRED EMBODIMENT
Fig. 1 shows a steam injector 1 according to the present invention. The steam injector 1 comprises a closed injector housing 2 of substantially tubular appearance.
The injector housing 2 displays an inlet 3 for a product which is to be heat treated in the injector 1, as well as an outlet 4 for the heat treated product. The injector housing 2 also has an inlet 5 for steam. The injector housing 2 is suitably manufactured from stainless steel so that it is suitable for use together with foods and so that it is easy to wash in an efficient manner.
Inside the injector housing 2, there is disposed an injector body 6 which is displaceable in the longitudinal direction of the injector housing 2. In the one end 7 of the injector body 6, there is disposed some form of regulator device (not shown).
The regulator device may be manual or automatic and, by displacing the injector body 6, it is thus possible to adjust the capacity of the injector 1.
At the other end of the injector body 6, there is placed a centre pin 8. The centre pin 8 and the injector housing 2 are designed so that concentric gaps are formed around the centre pin 8, of which at least one gap 9 is intended for product and at least one gap 10 is intended for steam. As a result of the adjustability of the injector body 6, it is possible to regulate the gap 9 for the product flow, as shown in Fig. 2A and 2B. Both the centre pin 8 and the injector body 6 are suitably manufactured from stainless steel, so that they are suitable for use with foods and so that they are easy to wash in an efficient manner.
The centre pin 8 is, according to the invention, formed so that the first part 11 most proximal the injector body 2 is conical in such a manner that the diameter dimension of the centre pin 8 increases in relation to the diameter dimension of the injector body 6. Moreover, on this first part 11 of the centre pin a number of grooves 12 start which are milled in the circumferential surface of the centre pin 8.
The second part 13 of the centre pin 8 is straight, and on this part 13 the grooves 12 continue, partly as straight grooves, i.e. they are axially directed. On the other hand, the grooves 12 begin to turn on this part 13. The grooves 12 are turned through 30-40° and preferably 35° in relation to the longitudinal direction of the injector body 2 and the centre pin 8. This turning is shown in Fig.4 as the angle a.
The third part 14 of the centre pin 8 is once again conical with reducing diameter from the diameter of the straight, second part 13. The grooves 12 continue with the same turn throughout the entire circumferential surface of the third part 14. The grooves 12 are, in the preferred embodiment, between 5 and 30 in number, preferably 20 in number, uniformly distributed over the centre pin 8. The number of grooves 12 depends upon capacity and the width of the grooves 12. The preferred number of grooves 12 gives a distribution angle of 18°, which is shown in
Fig. 5 by means of the angle β. The number of grooves 12 may be varied and may be more or fewer than 20 in number. Another number of grooves 12 than in the preferred embodiment would naturally give a different distribution angle.
The grooves 12 have a width of 0.5-5 mm and a depth of 0.8-3.5 mm. The grooves preferably display a square, or alternatively rectangular cross section, but other types of cross section may also be employed. In the preferred embodiment, the grooves 12 have a square cross section with a width and depth of 3.5 mm. In the one end of the centre pin 8, there is disposed a guide cone 15. The guide cone 15 is placed in the outlet 4 for the heat-treated product. The purpose of the guide cone 15 is to control the mixing of product and steam out through the outlet 4. The product which enters into the injector 1 through the product inlet 3 may be a relatively viscous product, such as ice-cream mix, high fat content cream, puddings, soups, children's food or the like. The injector 1 may naturally also be employed for less viscous products.
The product which passes in through the inlet 3, into the injector housing 2, will, when it passes the first part 11 of the centre pin 8, be throttled in its flow which will assist in urging the product into the grooves 12 which start on this first part 11. The product then follows the centre pin 8 and the gap 9. As a result of the formation of the centre pin 8 and the turning of the grooves 12, an acceleration of the product will be obtained at the same time as the product is more formed as jets, rather than as a concentric column which is the case in conventional annular gap injectors.
The product jets converge with the steam which enters via the inlet 6 and then passes the gap 10. Given that the viscous product is finely divided into jets, an improved mixing will be obtained of product and steam which departs from the injector 1 through the outlet 4. With a centre pin 8 formed according to the present invention, stratification of product and steam will be avoided which could otherwise occur when use is made of a conventional annular gap injector for viscous products. The grooves 12 and their design also afford advantages as regards washing of the injector 1, since the washing liquid will be at a higher speed and be better distributed when it passes the centre pin 8. As a result of the efficient mixing of product and steam, there will be obtained a uniform and efficient heating of the product to the desired temperature. Since annular gap injectors do not give rise to serious fouling of product, there will at the same time be obtained long operational time, in particular for products showing a ready tendency to fouling, such as dairy produce of high viscosity or similar products.
As will have been apparent from the foregoing description, the present invention realises an adjustable steam injector which displays the advantages of conventional annular gap injectors as far as fouling is concerned, which thus affords long operational times. At the same time, the design of the injector gives an efficient mixing of product and steam so that there will be obtained a reliable and uniform heating of the product in the injector. The heating will be well defined and there will be obtained the desired bacteriological extermination.

Claims

WHAT IS CLAIMED IS:
1. An adjustable steam injector (1) comprising an injector housing (2) with an inlet (3) for a product, an outlet (4) for the product, as well as a steam inlet (5), the injector (1) further including an injector body (6) displaceable in the injector housing (2), said injector body (6) having, in its one end, a centre pin (8) around which are disposed concentric gaps (9, 10) for product and steam, respectively, characterised in that the centre pin (8) has a number of grooves (12) accommodated in its circumferential surface, the grooves (12) being turned towards the one end of the centre pin (8).
2. The adjustable steam injector as claimed in Claim 1, characterised in that the grooves (12) are between 5 and 30 in number.
3. The adjustable steam injector as claimed in Claim 2, characterised in that the grooves (12) are 20 in number.
4. The adjustable steam injector as claimed in Claim 1, characterised in that the centre pin (8) consists of three parts (11, 13, 14) of which the first part (11) is conical, the second part (13) is straight and the third part (14) is conical.
5. The adjustable steam injector as claimed in Claim 4, characterised in that the grooves (12) begin as axial grooves (12) on the first part (11), on the second part (13) the grooves (12) are first axial thereafter turned and, on the third part (14) the grooves (12) continue with the same turning throughout the entire third part (14).
6. The adjustable steam injector as claimed in any of the preceding Claims, characterised in that the grooves (12) have a width of 0.5-5 mm and a depth of 0.8-3.5 mm.
7. The adjustable steam injector as claimed in Claim 6, characterised in that the grooves (12) have a square cross section with a width and a depth of 3.5 mm.
PCT/SE2007/000995 2006-11-13 2007-11-12 Adjustable steam injector WO2008060218A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SESE0602408-7 2006-11-13
SE0602408A SE530567C2 (en) 2006-11-13 2006-11-13 Adjustable steam injector

Publications (1)

Publication Number Publication Date
WO2008060218A1 true WO2008060218A1 (en) 2008-05-22

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009105004A1 (en) * 2008-02-20 2009-08-27 Tetra Laval Holdings & Finance S.A. An adjustable steam injector
CN102327748A (en) * 2011-05-09 2012-01-25 戴拓 Middle and low pressure steam spraying liquefier
EP3927182A4 (en) * 2019-02-21 2022-10-19 Empirical Innovations, Inc. Heating medium injectors and injection methods for heating foodstuffs
WO2023104942A1 (en) * 2021-12-08 2023-06-15 Siccadania Engineering A/S Continuous vapor integrator

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1331163A (en) * 1961-08-19 1963-06-28 Escher Wyss Gmbh Device for starch gelation
EP0839461A1 (en) * 1996-10-31 1998-05-06 Societe Des Produits Nestle S.A. Process and apparatus for heating, pasteurising and sterilising of liquids
WO2002043848A1 (en) * 2000-11-29 2002-06-06 Tetra Laval Holdings & Finance Sa Variable steam injector

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1331163A (en) * 1961-08-19 1963-06-28 Escher Wyss Gmbh Device for starch gelation
EP0839461A1 (en) * 1996-10-31 1998-05-06 Societe Des Produits Nestle S.A. Process and apparatus for heating, pasteurising and sterilising of liquids
WO2002043848A1 (en) * 2000-11-29 2002-06-06 Tetra Laval Holdings & Finance Sa Variable steam injector

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009105004A1 (en) * 2008-02-20 2009-08-27 Tetra Laval Holdings & Finance S.A. An adjustable steam injector
EA017464B1 (en) * 2008-02-20 2012-12-28 Тетра Лаваль Холдингз Энд Файнэнс С.А. An adjustable steam injector
US10004244B2 (en) 2008-02-20 2018-06-26 Tetra Laval Holdings & Finance S.A. Adjustable steam injector
CN102327748A (en) * 2011-05-09 2012-01-25 戴拓 Middle and low pressure steam spraying liquefier
EP3927182A4 (en) * 2019-02-21 2022-10-19 Empirical Innovations, Inc. Heating medium injectors and injection methods for heating foodstuffs
US11864572B2 (en) 2019-02-21 2024-01-09 Empirical Innovations, Inc. Systems and methods for receiving the output of a direct steam injector
US11896040B2 (en) 2019-02-21 2024-02-13 Empirical Innovations, Inc. Articles including undenatured meat protein and water condensed from steam
WO2023104942A1 (en) * 2021-12-08 2023-06-15 Siccadania Engineering A/S Continuous vapor integrator

Also Published As

Publication number Publication date
SE0602408L (en) 2008-05-14
SE530567C2 (en) 2008-07-08

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