Uniform temperature roller system having uniform heat exchange by supercritical fluid

Abstract

A uniform temperature roller system for uniform temperature exchange by supercritical fluid is revealed. The system includes a roller body, a pair of rotary shafts, a plurality of heating/cooling modules and a supercritical fluid. The roller body includes a first chamber, a second chamber and a third chamber. The second chamber is a closed space and the two rotary shafts are formed on two lateral plates of a housing of the roller body correspondingly. The heating/cooling modules are mounted in the second chamber and the supercritical fluid is filled in the second chamber for transferring temperature between the heating/cooling modules and the roller shell. Thereby the uniform temperature roller system achieves heating or cooling quickly with uniform heat exchange so as to improve quality and yield rate of the product as well as extend service life of the roller.

Claims

1. A uniform temperature roller system for making a roller shell reach a uniform temperature using supercritical fluid comprising: a roller body which includes: a roller shell having an internal hollow portion divided into a first chamber, a second chamber, and a third chamber by a pair of separation plates wherein the second chamber is an enclosed space; a pair of rotary shafts which are disposed on two side plates of the roller shell, respectively; a plurality of heating/cooling modules mounted in the second chamber and each of which having two ends connected to the pair of the separation plates correspondingly; and a supercritical fluid which is filled into the second chamber and out of the plurality of heating/cooling modules to use for transferring temperature between the heating/cooling modules and the roller shell.

2. The system as claimed in claim 1, wherein the roller shell is made of metal.

3. The system as claimed in claim 1, wherein at least one of the heating/cooling modules is an electric-heating module.

4. The system as claimed in claim 3, wherein at least one of the electric heating modules is an induction heating module.

5. The system as claimed in claim 1, wherein at least one of the heating/cooling modules is a thermoelectric cooling module.

6. The system as claimed in claim 1, wherein at least one of the heating/cooling modules is a temperature exchange module for heating/cooling having two ends communicate with the first chamber and the third chamber, respectively; a channel is mounted in each of the rotary shafts for input and output of a temperature regulating medium; the channels communicate with the first chamber and the third chamber, respectively so that the temperature regulating medium flows into the first chamber through one of the rotary shafts for expansion in the first chamber effectively; then the temperature regulating medium passes through the temperature exchange module for heating/cooling to be gathered in the third chamber and flows out through the other rotary shaft.

7. The system as claimed in claim 6, wherein at least one of the temperature exchange modules for heating/cooling is provided with a plurality of heat exchange fins.

8. The system as claimed in claim 1, wherein the supercritical fluid is selected from the group consisting of carbon dioxide, water, methane, ethane, propane, ethylene, propene, methanol, ethanol, acetone and a combination thereof.

9. The system as claimed in claim 1, wherein a check valve is arranged at one of the side plates of the roller shell and communicating with the second chamber.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) The structure and the technical means adopted by the present invention to achieve the above and other objects can be best understood by referring to the following detailed description of the preferred embodiments and the accompanying drawings, wherein:

(2) FIG. 1 is a schematic view showing a conventional hot spiral roller for squeezing, pressing, or embossing;

(3) FIG. 2 is a schematic view showing a conventional hot drilled-in roller for squeezing, pressing, or embossing;

(4) FIG. 3 is a schematic view showing temperature distribution of a conventional hot spiral roller for squeezing, pressing, or embossing;

(5) FIG. 4 is a schematic drawing showing an embodiment squeezing and pressing an object on a platform according to the present invention;

(6) FIG. 5 is a sectional view of an embodiment of a uniform temperature roller system according to the present invention;

(7) FIG. 5A is a sectional view taken along line A-A of the embodiment in FIG. 5 using electric-heating modules as heating/cooling modules according to the present invention;

(8) FIG. 5B is a sectional view taken along line B-B of the embodiment in FIG. 5 using electric-heating modules as heating/cooling modules according to the present invention;

(9) FIG. 6 is a sectional view of an embodiment of a uniform temperature roller system using induction heating modules according to the present invention;

(10) FIG. 6A is a perspective view of an induction heating module according to the present invention;

(11) FIG. 7 is a sectional view of an embodiment of a uniform temperature roller system using thermoelectric cooling modules according to the present invention;

(12) FIG. 7A is a perspective view of a thermoelectric cooling module according to the present invention;

(13) FIG. 8 is a sectional view of an embodiment of a uniform temperature roller system using temperature exchange modules according to the present invention;

(14) FIG. 8A is a sectional view taken along line C-C of the embodiment in FIG. 8 according to the present invention;

(15) FIG. 8B is a sectional view taken along line D-D of the embodiment in FIG. 8 according to the present invention;

(16) FIG. 8C is a sectional view of the embodiment in FIG. 8 with a plurality of heat exchange fins according to the present invention.

DETAILED DESCRIPTION OF THE INVENTION

(17) Refer to FIG. 4, an embodiment of a uniform temperature roller system 20 for uniform temperature exchange by supercritical fluid applied to film squeezing and pressing equipment is provided. The uniform temperature roller system 20 can generate uniform heating during the heating process or uniform cooling during the cooling process. Moreover, the uniform temperature roller system 20 can be used alone or in combination with the pressure roller.

(18) The pressure roller is mainly used for generating contact pressure to effectively interact with an object (such as film) 50 to be processed, such as squeezing, pressing, embossing, cooling, heating, etc, during manufacturing and forming processes of the products.

(19) The pressure roller can be a conventional common pressure roller which is a rubber roller or a metal roller. The present uniform temperature roller system 20 can also be used as the pressure roller.

(20) The uniform temperature roller system 20 is used in combination with the pressure roller 10 to squeeze and press at least one object 50. Thereby the uniform temperature roller system 20 together with the pressure roller 10 holds the object 50 to be processed so that the object 50 can be manufactured effectively.

(21) During manufacturing of certain products, the uniform temperature roller system 20 can also be used alone (without the pressure roller). For example, the uniform temperature roller system 20 is used to act on an object 50 on a platform 40.

(22) As shown in FIG. 5, a uniform temperature roller system 20 includes a roller body 21, a pair of rotary shafts 22, a plurality of heating/cooling modules 23 and a supercritical fluid 70.

(23) The roller body 21 includes a cylindrical hollow roller shell 201. Generally, the roller body 21 is a metal roller. By a pair of separation plates 211, an internal hollow portion of the roller shell 201 is divided into a first chamber 212, a second chamber 213, and a third chamber 214, which are separated from one another. The second chamber 213 is a pressure-resistant closed space and mainly used for enabling the roller shell 201 of the roller body 21 to achieve a uniform temperature rapidly.

(24) In order to make the roller body 21 rotate, the two rotary shafts 22 are formed on two side plates 215 of the roller body 21.

(25) The heating/cooling modules 23 are mounted in the second chamber 213 and two ends of the respective heating/cooling modules 23 are connected to the pair of separation plates 211, respectively.

(26) In order to make the roller shell 201 of the roller body 21 reach a uniform temperature quickly, the second chamber 213 is filled with at least one supercritical fluid (SCF) 70 and the supercritical fluid 70 is out of the plurality of heating/cooling modules 23. With low surface tension, low viscosity and gas-like high diffusivity, the supercritical fluid 70 is used for transferring temperature (such as heat/cool) between the heating/cooling modules 23 and the roller shell 201.

(27) As shown in FIG. 5A and FIG. 5B, each of the heating/cooling modules 23 of the uniform temperature roller system 20 is an electric-heating module 231 which uses electric-heating material to generate heat. When a wire 202 provides power to the electric-heating module 231 and heat energy up to 200° C. is generated, the heat energy generated is diffused to the roller shell 201 uniformly and quickly by heat convection of the supercritical fluid 70 which involves molecular diffusion of the supercritical fluid 70. Thereby the roller shell 201 is evenly heated up to about 195° C. for heating the products to be processed.

(28) Refer to FIG. 6 and FIG. 6A, the electric heating module 231 mentioned above can also be an induction heating module 232 in which a magnetic field is generated and acted on a metal member 232b to generate heat energy when power is applied to a coil 232a.

(29) Refer to FIG. 7 and FIG. 7A, each of the heating/cooling modules 23 of the uniform temperature roller system 20 is a thermoelectric cooling module 233 which is a chip capable of absorbing heat to achieve the purpose of cooling. For example, the temperature of the thermoelectric cooling module 233 is negative five degrees Celsius (−5° C.). When the roller shell 201 is used to cool down the processed products whose temperature is 120° C., the heat absorbed is evenly and quickly diffused to the thermoelectric cooling modules 233 by heat convection of the supercritical fluid 70 which involves molecular diffusion of the supercritical fluid 70. Thereby the purpose of cooling is achieved rapidly.

(30) As shown in FIG. 8, FIG. 8A and FIG. 8C, the heating/cooling module 23 is designed to be a temperature exchange module 234 for heating/cooling besides the above electric heating module 231 and the thermoelectric cooling module 233. In order to improve heat exchange efficiency, at least one temperature exchange module 234 is further provided with a plurality of heat exchange fins 235 for increasing heat exchange area.

(31) Moreover, two ends of each temperature exchange module 234 communicate with the first chamber 212 and the third chamber 214, respectively. A channel 221 is mounted in each of the rotary shafts 22 for input and output of a temperature regulating medium 60. The channels 221 communicate with the first chamber 212 and the third chamber 214, respectively.

(32) The above temperature regulating medium 60 can be hot water, cold water, refrigerant, kerosene, etc. While in use, the temperature regulating medium 60 flows into the first chamber 212 through the channel 221 of one of the rotary shafts 22 for effective expansion in the space of the first chamber 212. Then the temperature regulating medium 60 passes through the temperature exchange modules 234 to be gathered in the third chamber 214 again. Lastly the temperature regulating medium 60 flows out through the channel 221 of the other rotary shaft 22. While the temperature regulating medium 60 flowing through the temperature exchange modules 234, heat exchange occurs between the temperature regulating medium 60 and the roller shell 201 by the supercritical fluid 70 in the second chamber 213 due to heat convection of the supercritical fluid 70 which involves molecular diffusion of the supercritical fluid 70.

(33) More specifically, the temperature regulating medium 60 with high heat capacity is required when the uniform temperature roller system 20 with the temperature exchange modules 234 is used to heat the products to be processed. For example, 100° C. hot water or 150° C. kerosene flows into the first chamber 212 through one of the rotary shafts 22 and passes through the temperature exchange modules 234. Thereby the heat is diffused quickly into the roller shell 201 through the supercritical fluid 70. Hence the roller shell 201 is heated and used for heating the products to be processed.

(34) While the uniform temperature roller system 20 with the temperature exchange modules 234 is used to cool the products to be processed, a low-temperature temperature regulating medium 60 such as 5° C. water or 5° C. kerosene is selected and used. The cold water or kerosene flows into the first chamber 212 through one of the rotary shafts 22 and passes through the temperature exchange module 234. Thereby the heat the roller shell 201 absorbed during the cooling of the 120° C. products to be processed is diffused quickly into the temperature exchange modules 234 through the supercritical fluid 70. Then heat exchange occurs again between the hot temperature exchange modules 234 and the cold temperature regulating medium 60. Thereby the cooling of the uniform temperature roller system 20 is achieved.

(35) The supercritical fluid 70 can be carbon dioxide, water, methane, ethane, propane, ethylene, propene, methanol, ethanol, acetone or their combinations. The respective supercritical fluids 70 have different critical temperatures. According to the working temperature of the uniform temperature roller system 20 required, different types of supercritical fluid 70 are selected and used.

(36) For effective replenishment, adjustment or replacement of the supercritical fluid 70, a check valve 216 is arranged at one of the side plates 215 of the roller body 21. The check valve 216 communicate with the second chamber 213 so that the supercritical fluid 70 in the second chamber 213 can be replenished, adjusted or replaced quickly by the check valve 216.

(37) The above description is only the preferred embodiments of the present invention, and is not intended to limit the present invention in any form. Although the invention has been disclosed as above in the preferred embodiments, they are not intended to limit the invention. A person skilled in the relevant art will recognize that equivalent embodiment modified and varied as equivalent changes disclosed above can be used without parting from the scope of the technical solution of the present invention. All the simple modification, equivalent changes and modifications of the above embodiments according to the material contents of the invention shall be within the scope of the technical solution of the present invention.