US20120006817A1 - Device for tempering - Google Patents
Device for tempering Download PDFInfo
- Publication number
- US20120006817A1 US20120006817A1 US13/176,467 US201113176467A US2012006817A1 US 20120006817 A1 US20120006817 A1 US 20120006817A1 US 201113176467 A US201113176467 A US 201113176467A US 2012006817 A1 US2012006817 A1 US 2012006817A1
- Authority
- US
- United States
- Prior art keywords
- container
- circulation line
- barrier
- liquid phase
- solid
- Prior art date
- Legal status (The legal status 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 status listed.)
- Abandoned
Links
- 238000005496 tempering Methods 0.000 title claims abstract description 7
- 239000007791 liquid phase Substances 0.000 claims abstract description 18
- 239000000203 mixture Substances 0.000 claims abstract description 13
- 239000007790 solid phase Substances 0.000 claims abstract description 13
- 239000002245 particle Substances 0.000 claims abstract description 9
- 235000013399 edible fruits Nutrition 0.000 claims abstract description 8
- 239000007788 liquid Substances 0.000 claims abstract description 6
- 239000007787 solid Substances 0.000 claims abstract description 5
- 230000004888 barrier function Effects 0.000 claims description 15
- 238000007872 degassing Methods 0.000 claims description 5
- 238000000605 extraction Methods 0.000 description 8
- 238000011049 filling Methods 0.000 description 7
- 239000000047 product Substances 0.000 description 6
- 230000007246 mechanism Effects 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 241001122767 Theaceae Species 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000010923 batch production Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 235000015203 fruit juice Nutrition 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000012263 liquid product Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000012265 solid product Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Images
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, 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
- A23L3/00—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
- A23L3/16—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by heating loose unpacked materials
Definitions
- the disclosure relates to a device for tempering a mixture of a solid and a liquid phase, particularly a liquid containing fruit particles, of the kind explained in the introductory portion of Claim 1 .
- Such a device is known from DE 39 30 934 A1.
- the known device contains a container that is heated via its wall, into which container the product portions to be processed, for example, fruit particles and juice, but also water, sugar, powder or the like, are introduced.
- the bottom side of the container is given an outlet of a circulation line that leads back into the upper area of the container via a heat exchanger.
- the container is likewise heated.
- a stirring mechanism that works against stationary arms rotates inside the container, whereby these arms extend from the container inner wall inwards in the direction of the stirring mechanism.
- the stirring mechanism is operated such that gravity separation takes place, whereby the liquid phase tends to collect on the bottom of the container and the solid components float.
- the liquid phase is predominantly drawn off from the bottom of the container and sent into the heat exchanger via a pump, whereby this heat exchanger further heats the liquid phase.
- the heated liquid subsequently ends up back in the container where it runs onto the floating fruit particles from above, as a result of which these floating fruit particles are likewise heated.
- One aspect of the disclosure is developing a device of the aforementioned type in a manner that is gentler on the product.
- the barrier is selected according to the type and consistency of the solid phase and is formed as a sieve in the simplest case.
- the barrier is preferably formed as an inner container and arranged at a distance from the wall of the container.
- the confluence of the tempered liquid phase into the container takes place from below and in that area of the container in which the solid phase is also located. This achieves a fast and deep mixing, so that the temperature in the container homogenizes very quickly.
- the temperature equalization inside the container can be further improved if the introduction of the tempered liquid phase takes place via a nozzle and consequently at a higher speed.
- the container according to the disclosure can preferably also be used in order to remove harmful gases, such as atmospheric oxygen, for example, from the mixture located in the container if a degassing device is provided.
- harmful gases such as atmospheric oxygen
- a device for creating positive pressure in the container allows the container to be emptied without the use of a pump, which frees the solid phase from a further mechanical load.
- the drawing shows a device 1 according to the disclosure that is formed in the embodiment shown for heating a mixture of a solid phase in the form of fruit particles and a liquid phase in the form of fruit juice or other liquids.
- the device according to the disclosure can, however, also be used for cooling the cited mixture or for tempering other mixtures that need to be handled carefully.
- the mixture can, for example, contain fruit particles in the form of pieces and/or fibers and/or cells; the liquids are present in the form of juice, tea, sugared water or the like.
- the device 1 contains a container 2 into which the components of the mixture are fed via a filling opening 3 in the upper area, whereby this container 2 contains an extraction point 4 at the deepest point through which the tempered mixture is drawn off.
- a circulation line 5 connects the container 2 to a heat exchanger 6 that is selected according to the product to be heated and that is preferably a plate heat exchanger.
- a pump 7 is furthermore connected in the circulation line 5 .
- the circulation line 5 leaves the container 2 via an exit point 5 a and enters into the container again via an entry point 5 b.
- the exit point 5 a of the circulation line 5 is separated from the interior of the container 2 by a barrier 8 that is formed such that only or predominantly the liquid phase enters into the circulation line 5 and consequently into the heat exchanger 6 and the pump 7 . In this way, it is ensured that the components of the solid phase are not excessively mechanically or thermally loaded.
- the manner of the barrier 8 is adapted to the solid phase that is to be held back, such as for example, its particle size and/or its consistency and/or its dimensional distribution (cells, fibers or pieces), so that the best possible retention effect can be achieved.
- the barrier 8 is formed as a sieve with an appropriate hole size.
- the barrier 8 can, however, also be a filter material or a membrane.
- the barrier 8 is preferably mechanically stiff, or stretched to be mechanically stiff, and is keep at a sufficient distance A from the exit point 5 a, which distance counteracts clogging.
- the barrier 8 is preferably formed as an inner container that runs coaxially to the container 2 and that is at a distance A from the same on all sides so that a collecting space 9 for the liquid phase forms between the barrier 8 and container 2 .
- the barrier 8 preferably spans the entire area of the container 2 taken up by the mixture under the outlet of the filling opening 3 and of the extraction point 4 preferably at least up to the intended maximum filling level.
- the exit point 5 a of the circulation line 5 lies in the collecting space 9 and is located as close as possible to the extraction point 4 so that the liquid phase can also be drawn off when the filling level in the container 2 is low.
- the entry point 5 b of the circulation line 5 into the container 2 lies outside the collecting space 9 in that area in which the solid phase that has been separated out is located.
- the entry point 5 b points upwards and is preferably given a nozzle 10 by means of which the tempered liquid phase is injected out of the heat exchanger 6 into the solid phase held back by the barrier 8 . Due to the introduction in the lower area of the container 2 , just above the extraction point 4 and essentially centred in the container 2 , the formation of bubbles or foaming due to the injection is also avoided. This approach also achieves good thermal distribution and the heat transfer between the heated (cooled) liquid phase is improved on its way up to the solid phase.
- the container 2 can furthermore be provided with a degassing device 11 and/or with a device 12 for creating positive pressure in the container 2 .
- a degassing device 11 For degassing, particularly for removing dissolved oxygen from the mixture/liquid phase, the interior of the container 2 can be set to negative pressure during or outside of the tempering process by the degassing device 11 .
- the container 2 can be set to positive pressure via the device 12 so that the container contents are pressed through the extraction point 4 .
- Both devices 11 , 12 preferably engage in the upper area of the container 2 , above the maximum filling level.
- discontinuous process (batch process) is preferred, the container can easily also be designed for continuous operation.
- a plurality of the above-described devices 1 are connected next to one another in parallel for effective operation and, for example, provided with a shared feed of the raw materials and a collecting line connected to all extraction points for withdrawing the tempered mixture.
- suitable cleaning devices and cleaning lines can be provided for cleaning at the end of operation or during operation.
- the device according to the disclosure can also be used for other mixed solid/liquid products that require especially careful handling of the solid phase.
- the device can be used both for heating and for cooling.
- additional filling openings or filling devices can be provided in order to add, for example, powder or other products, where applicable, also exactly dosed.
Abstract
A device for tempering a mixture of a solid and a liquid phase, particularly a liquid containing fruit particles, having a container that is connected to a heat exchanger via a circulation line where the circulation line has an entry point and exit point in the container. So that the device is gentler on the product, blocks the exit point of the circulation line from the solid phase is arranged in the container.
Description
- The present application claims the benefit of priority of German Application No. 102010031047.6, filed Jul. 7, 2011. The entire text of the priority application is incorporated herein by reference in its entirety.
- The disclosure relates to a device for tempering a mixture of a solid and a liquid phase, particularly a liquid containing fruit particles, of the kind explained in the introductory portion of
Claim 1. - Such a device is known from DE 39 30 934 A1. The known device contains a container that is heated via its wall, into which container the product portions to be processed, for example, fruit particles and juice, but also water, sugar, powder or the like, are introduced. The bottom side of the container is given an outlet of a circulation line that leads back into the upper area of the container via a heat exchanger. The container is likewise heated. A stirring mechanism that works against stationary arms rotates inside the container, whereby these arms extend from the container inner wall inwards in the direction of the stirring mechanism. The stirring mechanism is operated such that gravity separation takes place, whereby the liquid phase tends to collect on the bottom of the container and the solid components float. In this way, the liquid phase is predominantly drawn off from the bottom of the container and sent into the heat exchanger via a pump, whereby this heat exchanger further heats the liquid phase. The heated liquid subsequently ends up back in the container where it runs onto the floating fruit particles from above, as a result of which these floating fruit particles are likewise heated.
- Both the stirring mechanisms and the direct heating at the container wall represent a large load, however, particularly for sensitive products, and impair the quality.
- One aspect of the disclosure is developing a device of the aforementioned type in a manner that is gentler on the product.
- By means of the development according to the disclosure, a separation of the liquid phase or a great portion thereof is achieved that is substantially gentler on the product, whereby the liquid phase or a great portion thereof is then brought to the desired temperature without problems and returned again without a need for mechanical loading of the solid phase by the stirring mechanism used in the state of the art.
- The barrier is selected according to the type and consistency of the solid phase and is formed as a sieve in the simplest case.
- In order to create and maintain sufficient extraction space for the liquid phase, the barrier is preferably formed as an inner container and arranged at a distance from the wall of the container.
- The confluence of the tempered liquid phase into the container takes place from below and in that area of the container in which the solid phase is also located. This achieves a fast and deep mixing, so that the temperature in the container homogenizes very quickly.
- The temperature equalization inside the container can be further improved if the introduction of the tempered liquid phase takes place via a nozzle and consequently at a higher speed.
- If the confluence takes place from the bottom to the top, the homogenization of the temperature is further improved and accelerated.
- The container according to the disclosure can preferably also be used in order to remove harmful gases, such as atmospheric oxygen, for example, from the mixture located in the container if a degassing device is provided.
- A device for creating positive pressure in the container allows the container to be emptied without the use of a pump, which frees the solid phase from a further mechanical load.
- An embodiment of the disclosure is explained in more detail in the following drawing, which depicts the tempering device in schematic format.
- The drawing shows a
device 1 according to the disclosure that is formed in the embodiment shown for heating a mixture of a solid phase in the form of fruit particles and a liquid phase in the form of fruit juice or other liquids. The device according to the disclosure can, however, also be used for cooling the cited mixture or for tempering other mixtures that need to be handled carefully. - The mixture can, for example, contain fruit particles in the form of pieces and/or fibers and/or cells; the liquids are present in the form of juice, tea, sugared water or the like.
- The
device 1 contains a container 2 into which the components of the mixture are fed via afilling opening 3 in the upper area, whereby this container 2 contains anextraction point 4 at the deepest point through which the tempered mixture is drawn off. - A
circulation line 5 connects the container 2 to aheat exchanger 6 that is selected according to the product to be heated and that is preferably a plate heat exchanger. Apump 7 is furthermore connected in thecirculation line 5. Thecirculation line 5 leaves the container 2 via anexit point 5 a and enters into the container again via anentry point 5 b. - The
exit point 5 a of thecirculation line 5 is separated from the interior of the container 2 by abarrier 8 that is formed such that only or predominantly the liquid phase enters into thecirculation line 5 and consequently into theheat exchanger 6 and thepump 7. In this way, it is ensured that the components of the solid phase are not excessively mechanically or thermally loaded. - The manner of the
barrier 8 is adapted to the solid phase that is to be held back, such as for example, its particle size and/or its consistency and/or its dimensional distribution (cells, fibers or pieces), so that the best possible retention effect can be achieved. In the simplest case, which is sufficient in the majority of cases, thebarrier 8 is formed as a sieve with an appropriate hole size. Thebarrier 8 can, however, also be a filter material or a membrane. Thebarrier 8 is preferably mechanically stiff, or stretched to be mechanically stiff, and is keep at a sufficient distance A from theexit point 5 a, which distance counteracts clogging. Thebarrier 8 is preferably formed as an inner container that runs coaxially to the container 2 and that is at a distance A from the same on all sides so that a collecting space 9 for the liquid phase forms between thebarrier 8 and container 2. Thebarrier 8 preferably spans the entire area of the container 2 taken up by the mixture under the outlet of the filling opening 3 and of theextraction point 4 preferably at least up to the intended maximum filling level. - The
exit point 5 a of thecirculation line 5 lies in the collecting space 9 and is located as close as possible to theextraction point 4 so that the liquid phase can also be drawn off when the filling level in the container 2 is low. - The
entry point 5 b of thecirculation line 5 into the container 2 lies outside the collecting space 9 in that area in which the solid phase that has been separated out is located. Theentry point 5 b points upwards and is preferably given anozzle 10 by means of which the tempered liquid phase is injected out of theheat exchanger 6 into the solid phase held back by thebarrier 8. Due to the introduction in the lower area of the container 2, just above theextraction point 4 and essentially centred in the container 2, the formation of bubbles or foaming due to the injection is also avoided. This approach also achieves good thermal distribution and the heat transfer between the heated (cooled) liquid phase is improved on its way up to the solid phase. - The container 2 can furthermore be provided with a degassing device 11 and/or with a device 12 for creating positive pressure in the container 2. For degassing, particularly for removing dissolved oxygen from the mixture/liquid phase, the interior of the container 2 can be set to negative pressure during or outside of the tempering process by the degassing device 11.
- To create positive pressure in order, for example, to empty the container 2 via the
extraction point 4 in the gentlest possible manner, the container 2 can be set to positive pressure via the device 12 so that the container contents are pressed through theextraction point 4. - Both devices 11, 12 preferably engage in the upper area of the container 2, above the maximum filling level.
- Although the above described, discontinuous process (batch process) is preferred, the container can easily also be designed for continuous operation.
- In practical application, preferably a plurality of the above-described
devices 1 are connected next to one another in parallel for effective operation and, for example, provided with a shared feed of the raw materials and a collecting line connected to all extraction points for withdrawing the tempered mixture. Furthermore, suitable cleaning devices and cleaning lines can be provided for cleaning at the end of operation or during operation. - In modification of the described and drawn embodiment, the device according to the disclosure can also be used for other mixed solid/liquid products that require especially careful handling of the solid phase. The device can be used both for heating and for cooling. Furthermore, additional filling openings or filling devices can be provided in order to add, for example, powder or other products, where applicable, also exactly dosed.
Claims (9)
1. Device for tempering a mixture of a solid and a liquid phase, particularly a liquid containing fruit particles, comprising a container that is connected to a heat exchanger via a circulation line, wherein the circulation line opens into the container with an entry and an exit point, and a barrier that blocks the exit point of the circulation line from the solid phase is arranged in the container.
2. The device according to claim 1 , wherein the barrier is formed as a sieve.
3. The according to claim 1 , wherein the barrier arranged at a distance (A) to the wall of the container.
4. The device according to claim 1 , wherein the barrier formed as an inner container.
5. The device according to at claim 1 , wherein the entry point is arranged in the lower area of the container in the solid stage.
6. The device according to claim 1 , wherein the entry point of the circulation line contains a nozzle.
7. The device according to claim 1 , wherein the entry point points upwards.
8. The device according to claim 1 , and a degassing device is provided at the container.
9. The device according to claim 1 , and a device for creating a positive pressure in the container is provided.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102010031047A DE102010031047A1 (en) | 2010-07-07 | 2010-07-07 | Device for tempering |
DE102010031047.6 | 2010-07-07 |
Publications (1)
Publication Number | Publication Date |
---|---|
US20120006817A1 true US20120006817A1 (en) | 2012-01-12 |
Family
ID=44898240
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US13/176,467 Abandoned US20120006817A1 (en) | 2010-07-07 | 2011-07-05 | Device for tempering |
Country Status (8)
Country | Link |
---|---|
US (1) | US20120006817A1 (en) |
EP (1) | EP2404510B1 (en) |
CN (1) | CN102334915B (en) |
BR (1) | BRPI1103249A2 (en) |
DE (1) | DE102010031047A1 (en) |
DK (1) | DK2404510T3 (en) |
ES (1) | ES2389560T3 (en) |
PL (1) | PL2404510T3 (en) |
Citations (94)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1842969A (en) * | 1929-11-09 | 1932-01-26 | Wilbert A Heyman | Packaging liquids |
US2035619A (en) * | 1934-04-20 | 1936-03-31 | Harry J Porter | Process of treating fruit juices |
US2052396A (en) * | 1934-11-09 | 1936-08-25 | Trumbull Electric Mfg Co | Electric heating of liquids |
US2297190A (en) * | 1939-10-11 | 1942-09-29 | Ronald B Mckinnis | Apparatus for packaging liquids |
US2388134A (en) * | 1938-06-24 | 1945-10-30 | Stokes Machine Co | Biological apparatus, container, and method |
US2562972A (en) * | 1944-11-14 | 1951-08-07 | Rca Corp | Method and apparatus for purifying and testing a fluid dielectric and filling a container or an electrical capacitor therewith |
US2639591A (en) * | 1948-04-29 | 1953-05-26 | Mojonnier Bros Co | Liquid cooling apparatus |
US2744629A (en) * | 1952-06-02 | 1956-05-08 | Rca Corp | Method and apparatus for processing chemicals |
US2934331A (en) * | 1955-12-22 | 1960-04-26 | Thomas J Walsh | Apparatus for making a metal slurry product |
US3000288A (en) * | 1957-05-15 | 1961-09-19 | Autolab Corp | Apparatus and method for processing photographic elements |
US3193991A (en) * | 1963-09-25 | 1965-07-13 | Joe L Browning | Continuous mixing apparatus |
US3326530A (en) * | 1964-06-01 | 1967-06-20 | Swift & Co | Apparatus for dispensing and mixing measured amounts of liquid |
US3395634A (en) * | 1965-01-15 | 1968-08-06 | Hupp Corp | Coffee roasting apparatus |
US3586510A (en) * | 1969-06-13 | 1971-06-22 | Us Agriculture | Helical pump system and use in processing of foods |
US3605828A (en) * | 1970-04-01 | 1971-09-20 | Cpc International Inc | Pilot bottling and canning unit |
US3621892A (en) * | 1969-09-04 | 1971-11-23 | Thomas J Gillespie | Resin vacuum degassing and dispensing system and method |
US3873753A (en) * | 1970-05-26 | 1975-03-25 | Purdue Research Foundation | Method for processing and storing tomatoes |
US3999474A (en) * | 1973-09-10 | 1976-12-28 | General Foods Corporation | Apparatus for producing a meat analog |
US4214013A (en) * | 1979-03-05 | 1980-07-22 | Fmc Corporation | Continuous pressure cooking method |
US4234605A (en) * | 1977-08-19 | 1980-11-18 | Shigeo Takeuchi | Method of making bread in an oven using a combined trough and baking-pan unit |
US4256773A (en) * | 1977-11-07 | 1981-03-17 | Takeda Chemical Industries, Ltd. | Brominated carbonaceous molecular sieve and method of use therefor |
US4307062A (en) * | 1978-11-16 | 1981-12-22 | The Upjohn Company | Particulate-containing foamed plastic |
US4306493A (en) * | 1978-10-05 | 1981-12-22 | Alpma Alpenland Maschinenbau Hain & Co. Kg | Device for washing and cooling the granulate of cottage cheese, curd or the like |
US4307760A (en) * | 1977-11-02 | 1981-12-29 | Wilhelm Hedrich Vakuumanlagen Gmbh & Co. Kg | Pressure-regulated mold-filling apparatus for thermosetting material |
US4344859A (en) * | 1975-01-08 | 1982-08-17 | Exxon Research And Engineering Company | Homogenizing system for producing high polymer latices |
US4360046A (en) * | 1980-06-09 | 1982-11-23 | Streit Philip N | Sanitary waste grease disposal apparatus |
US4361083A (en) * | 1979-12-28 | 1982-11-30 | Societe D'assistance Technique Pour Produits Nestle S.A. | Apparatus for treating a foodstuff |
US4421020A (en) * | 1981-05-22 | 1983-12-20 | The J. M. Smucker Company | Apparatus for the concentration of fruits |
US4446781A (en) * | 1981-03-21 | 1984-05-08 | Luwa Ag | Apparatus for the mechanical/thermal treatment, including sterilization and pasteurization, of fluids |
US4538509A (en) * | 1983-08-22 | 1985-09-03 | Hosiden Electronics Co., Ltd. | Automatic bread baking machine |
US4547383A (en) * | 1983-06-07 | 1985-10-15 | Campbell Soup Company | Continuous food sterilization system with hydrostatic sealed treatment chamber |
US4567749A (en) * | 1983-04-20 | 1986-02-04 | Commissariat A L'energie Atomique | Process and apparatus for determining the interfacial area in a two-phase mixture incorporating a gaseous phase flowing in the form of bubbles |
US4620962A (en) * | 1985-03-04 | 1986-11-04 | Mg Industries | Method and apparatus for providing sterilized cryogenic liquids |
US4679498A (en) * | 1983-08-26 | 1987-07-14 | Clextral | Installation for preparing a chocolate paste |
US4689237A (en) * | 1982-11-24 | 1987-08-25 | Institute National De La Recherche Agronomique | Process for the thermal treatment of fluids |
US4738193A (en) * | 1985-02-04 | 1988-04-19 | Heat And Control, Inc. | Food processing method and apparatus |
US4747517A (en) * | 1987-03-23 | 1988-05-31 | Minnesota Mining And Manufacturing Company | Dispenser for metering proportionate increments of polymerizable materials |
US4765745A (en) * | 1984-06-22 | 1988-08-23 | Werner & Pfleiderer | Apparatus for dosing and mixing solids and liquids to form a low viscosity suspension |
US4830278A (en) * | 1987-09-12 | 1989-05-16 | Nissen Corporation | Steam sterilizing apparatus |
US4838154A (en) * | 1985-05-31 | 1989-06-13 | Maxwell Laboratories, Inc. | Apparatus for extending the shelf life of fluid food products |
US4846054A (en) * | 1985-04-17 | 1989-07-11 | Clextral | Apparatus for extracting fat from an animal material |
US4856289A (en) * | 1988-07-08 | 1989-08-15 | Lofland Spencer G | Apparatus for reclaiming and purifying chlorinated fluorocarbons |
US4901632A (en) * | 1987-11-27 | 1990-02-20 | Giulio Lori | Three-phase process and machine for cooking foods as dry pasta, rice, legumes and the like |
US4921719A (en) * | 1987-06-11 | 1990-05-01 | Bowater Packaging Limited | Method and apparatus for the continuous preservation of lumpy products such as food product in lump form |
US4924764A (en) * | 1985-08-09 | 1990-05-15 | Otto Hansel Gmbh | Method and device for the batchwise production of aerated sweets in a pressure-beating machine |
US4942808A (en) * | 1985-02-04 | 1990-07-24 | Heat And Control, Inc. | Food processing apparatus |
US4969495A (en) * | 1989-06-27 | 1990-11-13 | Grant David C H | Direct condensation refrigerant recovery and restoration system |
US5038838A (en) * | 1989-01-04 | 1991-08-13 | Nuovopignone-Industrie Meccaniche E Fonderia S.P.A. | System for safe vapour recovery, particularly suitable for fuel filling installations |
US5048404A (en) * | 1985-05-31 | 1991-09-17 | Foodco Corporation | High pulsed voltage systems for extending the shelf life of pumpable food products |
US5088526A (en) * | 1989-12-07 | 1992-02-18 | Nash John P | Method for disposal of aerosol spray containers |
US5094277A (en) * | 1989-06-27 | 1992-03-10 | Ashland Oil Inc. | Direct condensation refrigerant recovery and restoration system |
US5156020A (en) * | 1989-11-29 | 1992-10-20 | The Boc Group Plc | Cooling apparatus |
US5203177A (en) * | 1991-11-25 | 1993-04-20 | Spx Corporation | Refrigerant handling system with inlet refrigerant liquid/vapor flow control |
US5235905A (en) * | 1985-05-31 | 1993-08-17 | Foodco Corporation | High pulsed voltage systems for extending the shelf life of pumpable food products |
US5344231A (en) * | 1990-02-19 | 1994-09-06 | Gambro Ab | System for the preparation of a fluid concentrate intended for medical use |
US5360139A (en) * | 1993-01-22 | 1994-11-01 | Hydra Rig, Inc. | Liquified natural gas fueling facility |
US5360622A (en) * | 1989-03-02 | 1994-11-01 | Ryosuke Yokoyama | Method and apparatus for kneading powder, and kneaded material |
US5368093A (en) * | 1992-11-25 | 1994-11-29 | Sanwa Life Cela Kabushiki Kaisha | Thawing device for frozen foods |
US5374435A (en) * | 1992-05-04 | 1994-12-20 | Imdec, S.A. | Method of batch cooking and packing fruit and vegetable pieces |
US5393541A (en) * | 1994-01-06 | 1995-02-28 | Foodco Corporation | Prevention of electrode fouling in high electric field systems for killing microorganisms in food products |
US5398734A (en) * | 1992-09-26 | 1995-03-21 | Khs Maschinen- Und Anlagenbau Aktiengesellschaft | Apparatus for monitoring the thermal treatment or sterilization of bottles or similar containers in a container-treatment machine |
US5411715A (en) * | 1992-06-09 | 1995-05-02 | Eastman Kodak Company | Apparatus for preparing aqueous amorphous particle dispersions of high-melting microcrystalline solids |
US5419239A (en) * | 1990-10-09 | 1995-05-30 | Ore-Ida Foods, Inc. | Automatic air heating system for vending machines |
US5468508A (en) * | 1991-10-17 | 1995-11-21 | The University Of British Columbia | Preservation of fresh fruit juices and fruit juice blends |
US5472275A (en) * | 1992-07-10 | 1995-12-05 | Societe De Construction | Assembly for the continuous plasticising and filtration of materials |
US5511875A (en) * | 1990-02-19 | 1996-04-30 | Gambro Ab | System for the preparation of a fluid concentrate intended for medical use |
US5527974A (en) * | 1992-02-05 | 1996-06-18 | Henkel Kommanditgesellschaft Auf Aktien | Process for the purification of glycerol water |
US5582016A (en) * | 1992-05-07 | 1996-12-10 | Aerospace Design & Development, Inc. | Conditioning and loading apparatus and method for gas storage at cryogenic temperature and supercritical pressure |
US5672374A (en) * | 1995-11-15 | 1997-09-30 | Environmental Liquid Reclamation, Inc. | Process and apparatus for producing a food product |
US5693119A (en) * | 1995-10-10 | 1997-12-02 | The Penn State Research Foundation | Solid-phase P buffer for sustained low-leaching P fertilization of plants |
US5727450A (en) * | 1995-03-14 | 1998-03-17 | Vassiliou; Eustathios | Apparatus for making artificial egg yolks in the form of a cylinder |
US5762119A (en) * | 1996-11-29 | 1998-06-09 | Golden Spread Energy, Inc. | Cryogenic gas transportation and delivery system |
US5802961A (en) * | 1994-04-15 | 1998-09-08 | Fmc Corporation | Methods and apparatus for particulate heat exchange and transfer |
US5809911A (en) * | 1997-04-16 | 1998-09-22 | Allied Technology Group, Inc. | Multi-zone waste processing reactor system |
US5860737A (en) * | 1994-10-20 | 1999-01-19 | Eckhard Muller | Method for continuously mixing and degassing liquid |
US5957037A (en) * | 1996-02-06 | 1999-09-28 | Yorkshire Process Plant Limited | Heat exchange apparatus |
US6019033A (en) * | 1994-11-07 | 2000-02-01 | Frigoscandia, Inc. | Apparatus for steam pasteurization of food |
US6063336A (en) * | 1996-08-02 | 2000-05-16 | Westward Corporation | Method and apparatus for wood chip pasteurization |
US6073540A (en) * | 1998-11-10 | 2000-06-13 | Fmc Corporation | Apparatus for heating or cooling product containers |
US6084019A (en) * | 1996-12-31 | 2000-07-04 | Eastman Chemical Corporation | High I.V. polyester compositions containing platelet particles |
US6147337A (en) * | 1998-12-10 | 2000-11-14 | Aladdin Industries, Llc | Microwaveable heat retentive receptacle |
US6151911A (en) * | 1998-01-24 | 2000-11-28 | Bass Public Limited Company | Relating to cooling containers of beverages |
US6190461B1 (en) * | 1997-10-28 | 2001-02-20 | Semi-Bulk Systems, Inc. | Sugar liquification system and process |
US6220310B1 (en) * | 1997-07-22 | 2001-04-24 | Sidel | Method for filling containers and installation therefor |
US20020014276A1 (en) * | 2000-06-09 | 2002-02-07 | Ludwig Clusserath | Method of operating a machine for filling bottles, cans or the like beverage containers with a beverage, and a beverage container filling machine |
US6349850B1 (en) * | 1996-06-04 | 2002-02-26 | Societe De Conseils De Recherches Et D'applications Scientifiques Scras | Method for preparing an injectable preparation and device for implementing same |
US6389958B1 (en) * | 1999-07-21 | 2002-05-21 | Ono Foods Industrial Co., Ltd. | Heat cooking/sterilizing device |
US20020112776A1 (en) * | 2001-02-20 | 2002-08-22 | Nelson Patrick L. | Intermediate pressure dispensing method for a carbonated beverage |
US6530307B2 (en) * | 2001-02-16 | 2003-03-11 | Romar Llc | Cooking machine |
US20030051606A1 (en) * | 2001-02-16 | 2003-03-20 | Romar Llc | Cooking machine |
US6569482B2 (en) * | 1998-10-30 | 2003-05-27 | Excel Corporation | Method for surface treating animal tissue |
US20030101875A1 (en) * | 2000-05-08 | 2003-06-05 | Takuji Ono | Heating, cooking and sterilizing device |
US6581649B2 (en) * | 2001-07-13 | 2003-06-24 | L'air Liquide - Societe Anonyme A'directiore Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude | Methods and apparatus for delivering high purity liquids with low vapor pressure |
US6588458B2 (en) * | 2001-07-06 | 2003-07-08 | Icon Dynamics, Llc | System, apparatus and method for measuring and transferring the contents of a vessel |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2401764A1 (en) * | 1974-01-15 | 1975-07-24 | Metallwerk Ag Buchs Sg Buchs | Wine and fruit storage-treatment tanks - allow fully automatic operation whether empty or full |
DE3930934A1 (en) | 1988-11-18 | 1990-05-23 | Waldner Gmbh & Co Hermann | Processing small size fruits by defrosting in container - also used for thermal sterilisation and cooling to packaging temp. |
US4968516A (en) * | 1989-07-24 | 1990-11-06 | Thompson Neal W | Method and apparatus for cooking foodstuffs using auxiliary steam |
IT1288065B1 (en) * | 1996-12-23 | 1998-09-10 | Alessandro Bertocchi | PROCEDURE AND ENZYMATIC INACTIVATION SYSTEM INHERENT TO THE EXTRACTION OF JUICES OR PUREES FROM FOOD PRODUCTS |
CN2671475Y (en) * | 2003-12-24 | 2005-01-19 | 广东天际电器有限公司 | Water isolated heating type food stirrer |
-
2010
- 2010-07-07 DE DE102010031047A patent/DE102010031047A1/en not_active Withdrawn
-
2011
- 2011-04-11 PL PL11161883T patent/PL2404510T3/en unknown
- 2011-04-11 DK DK11161883.1T patent/DK2404510T3/en active
- 2011-04-11 EP EP11161883A patent/EP2404510B1/en active Active
- 2011-04-11 ES ES11161883T patent/ES2389560T3/en active Active
- 2011-07-05 BR BRPI1103249-9A patent/BRPI1103249A2/en not_active Application Discontinuation
- 2011-07-05 US US13/176,467 patent/US20120006817A1/en not_active Abandoned
- 2011-07-06 CN CN201110192960.9A patent/CN102334915B/en not_active Expired - Fee Related
Patent Citations (99)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1842969A (en) * | 1929-11-09 | 1932-01-26 | Wilbert A Heyman | Packaging liquids |
US2035619A (en) * | 1934-04-20 | 1936-03-31 | Harry J Porter | Process of treating fruit juices |
US2052396A (en) * | 1934-11-09 | 1936-08-25 | Trumbull Electric Mfg Co | Electric heating of liquids |
US2388134A (en) * | 1938-06-24 | 1945-10-30 | Stokes Machine Co | Biological apparatus, container, and method |
US2297190A (en) * | 1939-10-11 | 1942-09-29 | Ronald B Mckinnis | Apparatus for packaging liquids |
US2562972A (en) * | 1944-11-14 | 1951-08-07 | Rca Corp | Method and apparatus for purifying and testing a fluid dielectric and filling a container or an electrical capacitor therewith |
US2639591A (en) * | 1948-04-29 | 1953-05-26 | Mojonnier Bros Co | Liquid cooling apparatus |
US2744629A (en) * | 1952-06-02 | 1956-05-08 | Rca Corp | Method and apparatus for processing chemicals |
US2934331A (en) * | 1955-12-22 | 1960-04-26 | Thomas J Walsh | Apparatus for making a metal slurry product |
US3000288A (en) * | 1957-05-15 | 1961-09-19 | Autolab Corp | Apparatus and method for processing photographic elements |
US3193991A (en) * | 1963-09-25 | 1965-07-13 | Joe L Browning | Continuous mixing apparatus |
US3326530A (en) * | 1964-06-01 | 1967-06-20 | Swift & Co | Apparatus for dispensing and mixing measured amounts of liquid |
US3395634A (en) * | 1965-01-15 | 1968-08-06 | Hupp Corp | Coffee roasting apparatus |
US3586510A (en) * | 1969-06-13 | 1971-06-22 | Us Agriculture | Helical pump system and use in processing of foods |
US3621892A (en) * | 1969-09-04 | 1971-11-23 | Thomas J Gillespie | Resin vacuum degassing and dispensing system and method |
US3605828A (en) * | 1970-04-01 | 1971-09-20 | Cpc International Inc | Pilot bottling and canning unit |
US3873753A (en) * | 1970-05-26 | 1975-03-25 | Purdue Research Foundation | Method for processing and storing tomatoes |
US3999474A (en) * | 1973-09-10 | 1976-12-28 | General Foods Corporation | Apparatus for producing a meat analog |
US4344859A (en) * | 1975-01-08 | 1982-08-17 | Exxon Research And Engineering Company | Homogenizing system for producing high polymer latices |
US4234605A (en) * | 1977-08-19 | 1980-11-18 | Shigeo Takeuchi | Method of making bread in an oven using a combined trough and baking-pan unit |
US4307760A (en) * | 1977-11-02 | 1981-12-29 | Wilhelm Hedrich Vakuumanlagen Gmbh & Co. Kg | Pressure-regulated mold-filling apparatus for thermosetting material |
US4256773A (en) * | 1977-11-07 | 1981-03-17 | Takeda Chemical Industries, Ltd. | Brominated carbonaceous molecular sieve and method of use therefor |
US4306493A (en) * | 1978-10-05 | 1981-12-22 | Alpma Alpenland Maschinenbau Hain & Co. Kg | Device for washing and cooling the granulate of cottage cheese, curd or the like |
US4307062A (en) * | 1978-11-16 | 1981-12-22 | The Upjohn Company | Particulate-containing foamed plastic |
US4214013A (en) * | 1979-03-05 | 1980-07-22 | Fmc Corporation | Continuous pressure cooking method |
US4361083A (en) * | 1979-12-28 | 1982-11-30 | Societe D'assistance Technique Pour Produits Nestle S.A. | Apparatus for treating a foodstuff |
US4360046A (en) * | 1980-06-09 | 1982-11-23 | Streit Philip N | Sanitary waste grease disposal apparatus |
US4446781A (en) * | 1981-03-21 | 1984-05-08 | Luwa Ag | Apparatus for the mechanical/thermal treatment, including sterilization and pasteurization, of fluids |
US4421020A (en) * | 1981-05-22 | 1983-12-20 | The J. M. Smucker Company | Apparatus for the concentration of fruits |
US4689237A (en) * | 1982-11-24 | 1987-08-25 | Institute National De La Recherche Agronomique | Process for the thermal treatment of fluids |
US4567749A (en) * | 1983-04-20 | 1986-02-04 | Commissariat A L'energie Atomique | Process and apparatus for determining the interfacial area in a two-phase mixture incorporating a gaseous phase flowing in the form of bubbles |
US4547383A (en) * | 1983-06-07 | 1985-10-15 | Campbell Soup Company | Continuous food sterilization system with hydrostatic sealed treatment chamber |
US4538509A (en) * | 1983-08-22 | 1985-09-03 | Hosiden Electronics Co., Ltd. | Automatic bread baking machine |
US4679498A (en) * | 1983-08-26 | 1987-07-14 | Clextral | Installation for preparing a chocolate paste |
US4765745A (en) * | 1984-06-22 | 1988-08-23 | Werner & Pfleiderer | Apparatus for dosing and mixing solids and liquids to form a low viscosity suspension |
US4738193A (en) * | 1985-02-04 | 1988-04-19 | Heat And Control, Inc. | Food processing method and apparatus |
US4942808A (en) * | 1985-02-04 | 1990-07-24 | Heat And Control, Inc. | Food processing apparatus |
US4620962A (en) * | 1985-03-04 | 1986-11-04 | Mg Industries | Method and apparatus for providing sterilized cryogenic liquids |
US4846054A (en) * | 1985-04-17 | 1989-07-11 | Clextral | Apparatus for extracting fat from an animal material |
US4838154A (en) * | 1985-05-31 | 1989-06-13 | Maxwell Laboratories, Inc. | Apparatus for extending the shelf life of fluid food products |
US5235905A (en) * | 1985-05-31 | 1993-08-17 | Foodco Corporation | High pulsed voltage systems for extending the shelf life of pumpable food products |
US5048404A (en) * | 1985-05-31 | 1991-09-17 | Foodco Corporation | High pulsed voltage systems for extending the shelf life of pumpable food products |
US4924764A (en) * | 1985-08-09 | 1990-05-15 | Otto Hansel Gmbh | Method and device for the batchwise production of aerated sweets in a pressure-beating machine |
US4747517A (en) * | 1987-03-23 | 1988-05-31 | Minnesota Mining And Manufacturing Company | Dispenser for metering proportionate increments of polymerizable materials |
US4921719A (en) * | 1987-06-11 | 1990-05-01 | Bowater Packaging Limited | Method and apparatus for the continuous preservation of lumpy products such as food product in lump form |
US4830278A (en) * | 1987-09-12 | 1989-05-16 | Nissen Corporation | Steam sterilizing apparatus |
US4901632A (en) * | 1987-11-27 | 1990-02-20 | Giulio Lori | Three-phase process and machine for cooking foods as dry pasta, rice, legumes and the like |
US4856289A (en) * | 1988-07-08 | 1989-08-15 | Lofland Spencer G | Apparatus for reclaiming and purifying chlorinated fluorocarbons |
US5038838A (en) * | 1989-01-04 | 1991-08-13 | Nuovopignone-Industrie Meccaniche E Fonderia S.P.A. | System for safe vapour recovery, particularly suitable for fuel filling installations |
US5360622A (en) * | 1989-03-02 | 1994-11-01 | Ryosuke Yokoyama | Method and apparatus for kneading powder, and kneaded material |
US4969495A (en) * | 1989-06-27 | 1990-11-13 | Grant David C H | Direct condensation refrigerant recovery and restoration system |
US5094277A (en) * | 1989-06-27 | 1992-03-10 | Ashland Oil Inc. | Direct condensation refrigerant recovery and restoration system |
US5156020A (en) * | 1989-11-29 | 1992-10-20 | The Boc Group Plc | Cooling apparatus |
US5088526A (en) * | 1989-12-07 | 1992-02-18 | Nash John P | Method for disposal of aerosol spray containers |
US5511875A (en) * | 1990-02-19 | 1996-04-30 | Gambro Ab | System for the preparation of a fluid concentrate intended for medical use |
US5344231A (en) * | 1990-02-19 | 1994-09-06 | Gambro Ab | System for the preparation of a fluid concentrate intended for medical use |
US5348389A (en) * | 1990-02-19 | 1994-09-20 | Gambro, Ab | System for the preparation of a fluid concentrate intended for medical use |
US6149294A (en) * | 1990-02-19 | 2000-11-21 | Gambro Ab | System for the preparation of a fluid concentrate intended for medical use |
US5419239A (en) * | 1990-10-09 | 1995-05-30 | Ore-Ida Foods, Inc. | Automatic air heating system for vending machines |
US5468508A (en) * | 1991-10-17 | 1995-11-21 | The University Of British Columbia | Preservation of fresh fruit juices and fruit juice blends |
US5203177A (en) * | 1991-11-25 | 1993-04-20 | Spx Corporation | Refrigerant handling system with inlet refrigerant liquid/vapor flow control |
US5527974A (en) * | 1992-02-05 | 1996-06-18 | Henkel Kommanditgesellschaft Auf Aktien | Process for the purification of glycerol water |
US5374435A (en) * | 1992-05-04 | 1994-12-20 | Imdec, S.A. | Method of batch cooking and packing fruit and vegetable pieces |
US5582016A (en) * | 1992-05-07 | 1996-12-10 | Aerospace Design & Development, Inc. | Conditioning and loading apparatus and method for gas storage at cryogenic temperature and supercritical pressure |
US5411715A (en) * | 1992-06-09 | 1995-05-02 | Eastman Kodak Company | Apparatus for preparing aqueous amorphous particle dispersions of high-melting microcrystalline solids |
US5472275A (en) * | 1992-07-10 | 1995-12-05 | Societe De Construction | Assembly for the continuous plasticising and filtration of materials |
US5398734A (en) * | 1992-09-26 | 1995-03-21 | Khs Maschinen- Und Anlagenbau Aktiengesellschaft | Apparatus for monitoring the thermal treatment or sterilization of bottles or similar containers in a container-treatment machine |
US5368093A (en) * | 1992-11-25 | 1994-11-29 | Sanwa Life Cela Kabushiki Kaisha | Thawing device for frozen foods |
US5360139A (en) * | 1993-01-22 | 1994-11-01 | Hydra Rig, Inc. | Liquified natural gas fueling facility |
US5393541A (en) * | 1994-01-06 | 1995-02-28 | Foodco Corporation | Prevention of electrode fouling in high electric field systems for killing microorganisms in food products |
US5802961A (en) * | 1994-04-15 | 1998-09-08 | Fmc Corporation | Methods and apparatus for particulate heat exchange and transfer |
US5860737A (en) * | 1994-10-20 | 1999-01-19 | Eckhard Muller | Method for continuously mixing and degassing liquid |
US6019033A (en) * | 1994-11-07 | 2000-02-01 | Frigoscandia, Inc. | Apparatus for steam pasteurization of food |
US5727450A (en) * | 1995-03-14 | 1998-03-17 | Vassiliou; Eustathios | Apparatus for making artificial egg yolks in the form of a cylinder |
US5693119A (en) * | 1995-10-10 | 1997-12-02 | The Penn State Research Foundation | Solid-phase P buffer for sustained low-leaching P fertilization of plants |
US5672374A (en) * | 1995-11-15 | 1997-09-30 | Environmental Liquid Reclamation, Inc. | Process and apparatus for producing a food product |
US5957037A (en) * | 1996-02-06 | 1999-09-28 | Yorkshire Process Plant Limited | Heat exchange apparatus |
US6349850B1 (en) * | 1996-06-04 | 2002-02-26 | Societe De Conseils De Recherches Et D'applications Scientifiques Scras | Method for preparing an injectable preparation and device for implementing same |
US6063336A (en) * | 1996-08-02 | 2000-05-16 | Westward Corporation | Method and apparatus for wood chip pasteurization |
US5762119A (en) * | 1996-11-29 | 1998-06-09 | Golden Spread Energy, Inc. | Cryogenic gas transportation and delivery system |
US6084019A (en) * | 1996-12-31 | 2000-07-04 | Eastman Chemical Corporation | High I.V. polyester compositions containing platelet particles |
US5809911A (en) * | 1997-04-16 | 1998-09-22 | Allied Technology Group, Inc. | Multi-zone waste processing reactor system |
US6220310B1 (en) * | 1997-07-22 | 2001-04-24 | Sidel | Method for filling containers and installation therefor |
US6190461B1 (en) * | 1997-10-28 | 2001-02-20 | Semi-Bulk Systems, Inc. | Sugar liquification system and process |
US6151911A (en) * | 1998-01-24 | 2000-11-28 | Bass Public Limited Company | Relating to cooling containers of beverages |
US6569482B2 (en) * | 1998-10-30 | 2003-05-27 | Excel Corporation | Method for surface treating animal tissue |
US6194015B1 (en) * | 1998-11-10 | 2001-02-27 | Fmc Corporation | Method for heating or cooling product containers |
US6073540A (en) * | 1998-11-10 | 2000-06-13 | Fmc Corporation | Apparatus for heating or cooling product containers |
US6147337A (en) * | 1998-12-10 | 2000-11-14 | Aladdin Industries, Llc | Microwaveable heat retentive receptacle |
US6389958B1 (en) * | 1999-07-21 | 2002-05-21 | Ono Foods Industrial Co., Ltd. | Heat cooking/sterilizing device |
US6626088B2 (en) * | 2000-05-08 | 2003-09-30 | Ono Foods Industrial Co., Ltd. | Heating, cooking and sterilizing device |
US20030101875A1 (en) * | 2000-05-08 | 2003-06-05 | Takuji Ono | Heating, cooking and sterilizing device |
US20020014276A1 (en) * | 2000-06-09 | 2002-02-07 | Ludwig Clusserath | Method of operating a machine for filling bottles, cans or the like beverage containers with a beverage, and a beverage container filling machine |
US6463964B2 (en) * | 2000-06-09 | 2002-10-15 | Khs Maschinen- Und Anlagenbau Ag | Method of operating a machine for filling bottles, cans or the like beverage containers with a beverage, and a beverage container filling machine |
US20030051606A1 (en) * | 2001-02-16 | 2003-03-20 | Romar Llc | Cooking machine |
US6530307B2 (en) * | 2001-02-16 | 2003-03-11 | Romar Llc | Cooking machine |
US20020112776A1 (en) * | 2001-02-20 | 2002-08-22 | Nelson Patrick L. | Intermediate pressure dispensing method for a carbonated beverage |
US6588458B2 (en) * | 2001-07-06 | 2003-07-08 | Icon Dynamics, Llc | System, apparatus and method for measuring and transferring the contents of a vessel |
US6581649B2 (en) * | 2001-07-13 | 2003-06-24 | L'air Liquide - Societe Anonyme A'directiore Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude | Methods and apparatus for delivering high purity liquids with low vapor pressure |
Also Published As
Publication number | Publication date |
---|---|
CN102334915B (en) | 2014-01-22 |
EP2404510A1 (en) | 2012-01-11 |
DE102010031047A1 (en) | 2012-01-12 |
PL2404510T3 (en) | 2012-11-30 |
DK2404510T3 (en) | 2012-09-24 |
ES2389560T3 (en) | 2012-10-29 |
CN102334915A (en) | 2012-02-01 |
EP2404510B1 (en) | 2012-06-27 |
BRPI1103249A2 (en) | 2012-12-25 |
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Legal Events
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AS | Assignment |
Owner name: KRONES AG, GERMANY Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:RUNGE, TORSTEN;REEL/FRAME:026707/0276 Effective date: 20110726 |
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STCB | Information on status: application discontinuation |
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