Continuous heat treatment method for an electrically conductive fluid
10082338 ยท 2018-09-25
Assignee
Inventors
- Jean-Pierre Lucien Joseph Pain (Castelnau le Lez, FR)
- Stephanie Roux (Mollans sur Ouveze, FR)
- Mario Massa (Reggio Emilia, IT)
Cpc classification
A23L5/15
HUMAN NECESSITIES
F24H1/103
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Y10T137/6579
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
H05B3/60
ELECTRICITY
A23L3/005
HUMAN NECESSITIES
F28D15/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
H05B3/60
ELECTRICITY
A23L5/10
HUMAN NECESSITIES
F28D15/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
A23L3/005
HUMAN NECESSITIES
Abstract
A method is provided for heating an electrically conductive fluid, including steps of: (i) circulating the fluid in a circuit from an inlet to an outlet, through an inlet path of the circuit in which the fluid flows in a first average direction and an outlet path of the circuit in which the fluid flows in a second average direction substantially opposite to the first direction; (ii) subjecting the fluid to a specific ohmic heating while the fluid flows through the outlet path; and (iii) transferring heat from the fluid flowing through the outlet path to the fluid flowing through the inlet path by thermal conduction through an at least partially first electrically insulated partition wall. An associated heating device is also provided.
Claims
1. A method for heating an electrically conductive fluid comprising steps of: circulating the fluid in a circuit from an inlet to an outlet, through an inlet path of the circuit in which the fluid flows in a first average direction, and through an outlet path of the circuit in which the fluid flows in a second average direction substantially opposite to the first direction, wherein said inlet path has an inlet length extending from a first wall to a second wall, and said outlet path has an outlet length extending from said second wall to said first wall; subjecting the fluid to ohmic heating while the fluid flows through the outlet path; and transferring heat from the fluid flowing through the outlet path to the fluid flowing through the inlet path by thermal conduction through an electrically insulated partition wall separating said inlet path and said outlet path, wherein said electrically insulated partition wall extends along a majority of an entire length of said inlet length and said outlet length.
2. The method of claim 1, further comprising a step of subjecting the fluid to ohmic heating while said fluid flows through the inlet path.
3. The method of claim 1, further comprising at least one of the following steps: applying at least one voltage inducing ohmic heating in the fluid flowing through the inlet path between at least two electrodes arranged in said inlet path; and applying at least one voltage in the fluid flowing through the outlet path between at least two electrodes arranged in said outlet path.
4. The method of claim 3, further comprising at least one of the following steps: applying a first and a second voltage inducing ohmic heating in the fluid flowing through the inlet path, said first voltage being applied between a first electrode arranged substantially toward a first axial end of the inlet path and a second electrode arranged substantially toward the middle of the inlet path, and said second voltage being applied between said second electrode and a third electrode arranged substantially toward a second axial end of the inlet path; and applying a third and a fourth voltage inducing ohmic heating in the fluid flowing through the outlet path, said third voltage being applied between a fourth electrode arranged substantially toward a first axial end of the outlet path and a fifth electrode arranged substantially toward the middle of the outlet path, and said fourth voltage being applied between said fifth electrode and a sixth electrode arranged substantially toward a second axial end of the outlet path.
5. The method of claim 1, further comprising a step of inducing ohmic heating in the fluid by applying AC voltage between electrodes at least partially in contact with the fluid.
6. The method of claim 1, further comprising a step of circulating the fluid through the inlet path at a higher average speed than through the outlet path.
7. The method of claim 1, further comprising a step of measuring the temperature of the fluid in at least one path among the inlet path and the outlet path.
8. The method of claim 1, wherein said first wall and said second wall are electrodes.
9. A method for heating an electrically conductive fluid comprising steps of: circulating the fluid in a circuit from an inlet to an outlet, through an inlet path of the circuit in which the fluid flows in a first average direction, and through an outlet path of the circuit in which the fluid flows in a second average direction substantially opposite to the first direction; subjecting the fluid to ohmic heating while the fluid flows through the outlet path; and providing an electrically insulated partition wall between said inlet path and said outlet path, wherein said partition wall extends along a majority of an entire length of said inlet length and said outlet length, said entire length defined between opposing ends of said inlet path and said outlet path, wherein no ohmic heating occurs through said partition wall; and transferring heat from the fluid flowing through the outlet path to the fluid flowing through the inlet path by thermal conduction through said electrically insulated partition wall.
Description
DESCRIPTION OF THE DRAWINGS
(1) The methods according to embodiments of the present invention may be better understood with reference to the drawings, which are given for illustrative purposes only and are not meant to be limiting. Other aspects, goals and advantages of the invention shall be apparent from the descriptions given hereunder.
(2)
(3)
(4)
(5)
(6)
(7) For clarity, identical or similar elements of the invention will be referenced with identical reference numbers in all figures.
DETAILED DESCRIPTION
(8)
(9) The paths are mutually positioned such that the first axial end 30 of the outlet path is axially located at the same axial position as the second axial end 20 of the inlet path, and in fluid connection with the latter. Moreover, the second axial end 40 of the outlet path is axially at the same axial position as the first axial end 10 of the inlet path.
(10) At least two electrodes 3,4 are located between the first end 10 and the second end 20 of the inlet path. According to this embodiment, these end electrodes 3,4 are located close to the first end 30 and the second end 40 of the outlet path. The end electrodes 3,4 located at the ends of the tubular external wall 2, allow an alternating electric current to be generated in the electrical conductive fluid to be treated and hence to heat it, as will be detailed later.
(11) Such an arrangement can be obtained through two coaxial tubular means 1, 2 wherein the inner tube 1 is a partition wall that radially encloses the outlet path. The external tubular means 2 radially encloses the inlet path.
(12) Both tubular means 1,2 are electrically insulated, and the inner or partition wall 1 is thus contiguous with both inlet and outlet paths as shown on
(13) The inner or partition wall 1 is made of a material having high thermal conductivity, and it has a rather small thickness in order to transfer heat as will be explained later.
(14) An electrically conductive fluid circulates from the inlet Ito the outlet O of the thus created circuit through an inlet path in which the fluid circulates in a first direction as illustrated by arrow A, and then through an outlet path where the fluid circulates in a second direction referenced by arrow B. The first direction A is opposite to the second direction B.
(15) The inlet I of the circuit is for example constituted by a channel through the first end electrode 4. The fluid flows firstly through the inlet path radially defined between the inner tube 1 and the outer tube 2, in the first direction A. The second end electrode 3 (voltage electrode) which is positioned at an axially end distance from the inner partition wall 1 has also the function of deviating the flow which thereafter circulates in the second direction B opposite to the first one A, all along and inside the inner tube 1. The electrically conductive fluid flows thus to the outlet O axially positioned near the inlet I and it is once more heated between second electrode 3 and first electrode 4 (grounded). The inner tube 1 is an electrically insulated partition wall such that heat is transferred by heat conduction from the fluid flowing through the outlet path to the fluid flowing through the inlet path.
(16) According to the embodiment illustrated in
(17) The arrangement is such that the inlet I is provided through the first electrode 4.
(18) The respective dimensions of the tubes 1,2, are such that the cross-section of the inlet path has nearly the same value as the cross-section of the outlet path. According to a preferred embodiment, the cross-section of the inlet path is lower than the cross-section of the outlet path.
(19) The second alternative creates bigger residence time for the fluid in the outlet path and consequently lower temperatures of the fluid in the inlet path, as well as lower wall temperatures as will be shown later on.
(20) According to an example, the thickness of the inner partition wall 1 is about 2.5 mm whereas the thickness of the tubular external wall 2 is about 8 mm. The external diameter of external wall 2 is about 50 mm whereas the external diameter of partition wall 1 is about 28 mm. In this example the fluid flow is about 150 l/h.
(21)
(22) It is interesting to point out that temperatures increase regularly and slowly from the input I to the output O of the circuit. Moreover, the partition wall temperature increases very slowly and regularly: from about 90 C. to 100 C. maximum. In other words, the partition wall 1 has an average temperature that slightly varies axially. This is an important advantage because this allows to considerably limit the clogging and/or fouling of the partition wall 1 by local overheating(s).
(23) The fluid pressure difference between input I and output O is very slim. This allows having thin thicknesses for the partition wall 1 which grants good heat transfer by conduction.
(24)
(25) In this embodiment, the cross-section of the inlet path can be equal to or lower than the cross-section of the outlet path.
(26)
(27) Another embodiment of the invention is shown on
(28) In this embodiment, the second axial end 20 of the inlet path is not in direct fluid connection with the first axial end 30 of the outlet path. The fluid, after flowing through the inlet path in direction A leaves the device through the intermediate outlet O, and the intermediate inlet I allows injecting it in the outlet path, so that it can flox in direction B.
(29) This embodiment allows cascading heating devices of the invention, with all inlet paths in series first, and then all outlet paths in series, along the path of the fluid. This is achieved by connecting the intermediate outlet O of the first heating device to the inlet I of the second heating device, and the outlet O of that second heating device to the intermediate inlet I of the first heating device, and so on for the next devices. The last heating device may be a device of the embodiment of
(30) By doing so, it is possible to build a heating system composed of a plurality of smaller heating devices which is functionally equivalent to a single large heating device with an inlet path and an outlet path whose lengths correspond to the sum of the lengths of the inlet paths and the outlet paths of the individual smaller heating devices, respectively.
(31) The same result may of course be achieved with modified systems based on the embodiment of
(32) Of course, the devices of the invention may also be cascaded so that an outlet O of a first device is connected to the inlet I of another device, and so on.
(33) At least one temperature sensor (non visible) is advantageously provided at least at inlet I and/or at outlet O of the circuit and it allows to continuously control the electrodes power and consequently the fluid temperature within the circuit.
(34) Besides, the inner partition wall 1 remains rather cold which generates a low viscosity parietal layer, the later one facilitates the fluid flowing therein. This layer provides a continuous lubrication of the inside of this wall which decreases pressure therein. A very nice flow is thus provided in the device according to the invention.
(35) Particularly, products with viscosities varying according to temperatures can be handled according to the invention: at fluid outlet, such products will show a high inside viscosity and a low outside viscosity. Viscosity increases when temperature decreases.
(36) For example at fluid outlet, a cake will be cooked at heart (inside) and will show a low viscosity outside. Sponge bread can be provided, without outside crust.
(37) As clearly appearing from the above specification, a single fluid circuit is used which significantly simplify both the method and the device according to the invention.
(38) While this invention has been described in conjunction with a number of embodiments, it is evident that many alternatives, modifications and variations would be or are apparent to those of ordinary skill in the applicable arts. Accordingly, it is intended to embrace all such alternatives, modifications, equivalents and variations that are within the spirit and scope of this invention.