Scroll heating device

Abstract

A scroll heating device includes a base, a reaction region, and a first and a second channel. The reaction region is at the center of the base. The two channels are located on the base and extend spirally from the reaction region toward the periphery of the base. The width of each channel is gradually reduced as the channel extends from adjacent to the center of the base toward the periphery of the base. The first channel allows a gas that flows into the first channel through the periphery of the base toward the center of the base to flow toward the reaction region at a progressively slower rate, enter the reaction region slowly through the gradually widening first channel, and therefore stay in the reaction region for longer. The combusted exhaust enters the second channel from adjacent to the center of the base and exits through the periphery of the base.

Claims

1. A scroll heating device, comprising: a base; a reaction region located at a center of the base; and a first channel and a second channel, both located on the base and extending outward of the reaction region, where each of the first channel and the second channel extends spirally from a starting point defined by the reaction region toward a periphery of the base, and each of the first channel and the second channel has a width that is gradually reduced as each channel extends from a position adjacent to the center of the base toward the periphery of the base, such that both the first channel and the second channel become narrower toward the periphery of the base and wider toward the center of the base; wherein when a gas flows from a first end of the first channel that is located at the periphery of the base toward a second end of the first channel that is adjacent to the center of the base, the first channel allows the gas to flow toward the reaction region at a progressively slower rate and then enter the reaction region slowly through the first channel, which gradually widens toward the center of the base, thereby increasing a time for which the gas stays in the reaction region, and wherein a combusted exhaust flows into a third end of the second channel that is adjacent to the center of the base and exits through a fourth end of the second channel that is located at the periphery of the base.

2. The scroll heating device of claim 1, wherein the first channel and the second channel are arranged according to one or a combination of a Fermat's spiral configuration, a Vogel spiral configuration, and an Archimedean spiral configuration.

3. The scroll heating device of claim 2, wherein the base includes a gas inlet provided at the periphery of the base and in communication with the first channel and a gas outlet provided at the periphery of the base and in communication with the second channel, and the gas inlet and the gas outlet are located diametrically opposite each other.

4. The scroll heating device of claim 3, further comprising: a plurality of pin fins, wherein the base further includes two opposite sides defined respectively as a first side and a second side, the pin fins are located on the first side and are spaced apart from one another, and the first channel and the second channel are located on the second side.

5. The scroll heating device of claim 4, further comprising: a cover provided on the second side to close the first channel and the second channel.

6. The scroll heating device of claim 5, wherein the second end of the first channel is connected to the gas inlet, and the fourth end of the second channel is connected to the gas outlet.

7. The scroll heating device of claim 6, wherein the first side and the second side define therebetween a thickness of 3 mm.

8. The scroll heating device of claim 7, wherein the scroll heating device is made of a thermally conductive material, and the thermally conductive material is one or a combination selected from the group consisting of a metal, a metal alloy, and ceramic.

9. The scroll heating device of claim 8, wherein the gas is one or a combination selected from the group consisting of dimethyl ether (DME), methane (CH.sub.4), synthesis gas (syngas), natural gas, liquefied petroleum gas, and biogas.

10. The scroll heating device of claim 1, wherein the scroll heating device is adapted for being coupled to a heating end of a Stirling engine.

Description

BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS

(1) FIG. 1 is a perspective view of the scroll heating device according to a preferred embodiment of the present invention;

(2) FIG. 2 shows the scroll heating device in FIG. 1 from another viewing angle;

(3) FIG. 3 shows the scroll heating device in FIG. 1 from yet another viewing angle;

(4) FIG. 4 shows the routes of an ingoing gas and of the outgoing exhaust in the scroll heating device in FIG. 1;

(5) FIG. 5 is a sectional view taken along line A-A in FIG. 4;

(6) FIG. 6 shows how the scroll heating device in FIG. 1 and a Stirling engine are arranged with respect to each other; and

(7) FIG. 7 is a plot showing various electricity output states of the scroll heating device-and-Stirling engine assembly in FIG. 6.

DETAILED DESCRIPTION OF THE INVENTION

(8) The detailed description and preferred embodiments of the invention will be set forth in the following content, and provided for people skilled in the art to understand the characteristics of the invention.

(9) Referring to FIGS. 1-3, the scroll heating device 1 according to an embodiment of the present invention includes a base 11, a reaction region 12, a first channel 13, a second channel 14, a plurality of pin fins 15, and a cover 16. The scroll heating device 1 is adapted to be coupled to the heating end of a Stirling engine 9 (see FIG. 6).

(10) The scroll heating device 1 is made of a thermally conductive material. The thermally conductive material may be one or a combination selected from the group consisting of a metal, a metal alloy (preferably stainless steel, an aluminum alloy, etc.), and ceramic, and is preferably resistant to temperatures as high as 933 K. Due to its good thermal conductivity, the thermally conductive material can conduct heat to the Stirling engine 9 effectively. There is no limitation on the type of the fuel used in the scroll heating device 1. Various gaseous fuels, including those with a low heat value and difficult to burn directly, can be used, thus removing the conventional limitations on such low-heat-value fuels. Using this type of fuel helps achieve the objective of reusing energy in an effective manner. The gaseous fuel used in this embodiment (also referred to hereinafter as the fuel gas, or simply the gas) may be one or a combination selected from the group consisting of dimethyl ether (DME), methane (CH.sub.4), synthesis gas (syngas), natural gas, liquefied petroleum gas, biogas, and gasified biomass energy. DME is readily available. For example, biomass gas extracted from biomass can be used to produce CO and H.sub.2, which in turn can be processed into DME. DME is more portable than biomass gas, can be ignited with ease, and therefore has great potential as an alternative fuel.

(11) Referring to FIGS. 4-6, the base 11 includes a first side 111, an opposite second side 112, a gas inlet 113 provided at the periphery of the base 11 and in communication with the first channel 13, and a gas outlet 114 provided at the periphery of the base 11 and in communication with the second channel 14. The gas inlet 113 and the gas outlet 114 are located diametrically opposite each other. The fuel gas, or an unburned, room-temperature mixed gas to begin with, is input into the scroll heating device 1 through the gas inlet 113. The combusted, high-temperature exhaust, on the other hand, flows out of the scroll heating device 1 through the gas outlet 114. The input of the unburned gas and the output of the exhaust take place simultaneously.

(12) The base 11 defines a horizontal axis L1 that passes through the center point of the second side 112, a vertical axis L2 that is perpendicular to the horizontal axis L1 and passes through the center point of the base 11, and a center line L3 that penetrates the center point of the base 11.

(13) In this embodiment, the Stirling engine 9 is located on the first side 111 of the base 11. The thickness between the first side 111 and the second side 112 is 3 mm; in other words, the base 11 has a thickness of 3 mm.

(14) The reaction region 12 is located at the center of the base 11.

(15) The first channel 13 is located on the second side 112 of the base 11 and extends outward of the reaction region 12. More specifically, the first channel 13 extends spirally from a starting point defined by the reaction region 12 toward the periphery of the base 11. The width W1-W8 of the first channel 13 is gradually reduced as the first channel 13 extends from a position adjacent to the center of the base 11 toward the periphery of the base 11, meaning the first channel 13 becomes narrower toward the outer end, i.e., toward the periphery of the base 11, and wider toward the inner end, i.e., toward the center of the base 11.

(16) Similarly, the second channel 14 is located on the second side 112 of the base 11 and extends outward of the reaction region 12. More specifically, the second channel 14 extends spirally from a starting point defined by the reaction region 12 toward the periphery of the base 11. The width W1′-W8′ of the second channel 14 is gradually reduced as the second channel 14 extends from a position adjacent to the center of the base 11 toward the periphery of the base 11, meaning the second channel 14 becomes narrower toward the outer end, i.e., toward the periphery of the base 11, and wider toward the inner end, i.e., toward the center of the base 11.

(17) The first channel 13 has a first end 131 as its inner end, which is adjacent to the center of the base 11, and a second end 132 as its outer end, which is located away from the center of the base 11 and is connected to the gas inlet 113. The second channel 14 has a third end 141 as its inner end, which is adjacent to the center of the base 11, and a fourth end 142 as its outer end, which is located away from the center of the base 11 and is connected to the gas outlet 114.

(18) The first channel 13 and the second channel 14 may be arranged according to one or a combination of a Fermat's spiral configuration, a Vogel spiral configuration, and an Archimedean spiral configuration. In this embodiment, the first and the second channels 13 and 14 are arranged according to a Fermat's spiral configuration.

(19) More specifically, the width of the first channel 13 is gradually reduced from the center line L3 toward the periphery of the base 11, i.e., the width W1>the width W2>the width W3>the width W4>the width W5>the width W6>the width W7>the width W8, and the width of the second channel 14 is also gradually reduced from the center line L3 toward the periphery of the base 11, i.e., the width W1′>the width W2′>the width W3′>the width W4′>the width W5′>the width W6′>the width W7′>the width W8′.

(20) Furthermore, taking the center line L3 as the reference line, the left portions of the first and the second channels 13 and 14 and the right portions of the first and the second channels 13 and 14 are symmetric in width, i.e., the widths W1 and W1′ are the same, and so are the widths W2 and W2′, the widths W3 and W3′, the widths W4 and W4′, the widths W5 and W5′, the widths W6 and W6′, the widths W7 and W7′, and the widths W8 and W8′.

(21) The first channel 13 and the second channel 14 are provided on the second side 112 in an alternate manner Therefore, the portion of the ingoing gas that is moving toward the reaction region 12 along the outermost turn of the route R1 will be preheated by the hot exhaust in the turn of the route R2 that is on one side of the outermost turn of the route R1, and the portion of the ingoing gas that is moving along the second outermost turn of the route R1 will be preheated by the hot exhaust in the turns of the route R2 that immediately flank the second outermost turn of the route RE Thus, the gas moving in the first channel 13 will be continuously preheated by the exhaust on both sides of the first channel 13 (or on one side of the first channel 13 when the gas flows through the outermost turn of the route R1) until the reaction region 12 is reached, and an enhanced gas preheating effect is achieved. In particular, the portion of the exhaust that is moving along the innermost turn of the route R2 toward the gas outlet 114 has the highest temperature because it has just left the reaction region 12 for the gas outlet 114, and can therefore boost the preheating effect and optimize the efficiency of heat cycling by preheating the gas that is about to enter the reaction region 12, thereby reducing unnecessary heat dissipation, exergy destruction, and the additional energy required to preheat the reactants. The combustibility of the reactants will also be enhanced as a result, making it possible to burn low-heat-value fuels.

(22) The pin fins 15 are provided on the first side 111 and are spaced apart from one another to provide a plurality of contact surfaces and enhance a high convective heat transfer rate when heat is transferred through the contact surfaces to the working gas of the Stirling engine 9. The cover 16 is provided on the second side 112 to close the first and the second channels 13 and 14. As the thickness between the first side 111 and the second side 112 of the base 11 is merely 3 mm, and the first and the second channels 13 and 14 have outstanding heat transmitting and retaining abilities, heat can be transmitted from the gas in the first and the second channels 13 and 14 to the surfaces of the pin fins 15 rapidly. Thus, the aforementioned problem of the conventional heat exchangers, namely inefficient thermal conduction attributable to the limitations imposed on the mechanical structure and weight of a conventional heat exchanger, is solved. Furthermore, the scroll heating device 1 has a super thin design with an exceptionally high area/volume ratio, which increases the amount of heat that can be conducted.

(23) When the fuel gas flows from the second end 132 of the first channel 13 (which end is located at the periphery of the base 11) toward the first end 131 (which is adjacent to the center of the base 11), the first channel 13, which gradually narrows toward the outer end (i.e., the second end 132) and gradually widens toward the inner end (i.e., the first end 131), allows the gas to flow toward the reaction region 12 at a progressively slower rate and then enter the reaction region 12 slowly through the gradually widening first channel 13. As the flow velocity of the gas is reduced, the time for which the gas can stay and burn in the reaction region 12 is increased. Moreover, the gas moving in the first channel 13 is continuously preheated by the exhaust on both sides of the first channel 13 (or on one side of the first channel 13 when the gas flows through the outermost turn of the first channel 13) such that the gas preheating time and effect is enhanced to enable complete combustion.

(24) The combusted exhaust will flow into the third end 141 of the second channel 14 (which end is adjacent to the center of the base 11), exits through the fourth end 142 (which is located at the periphery of the base 11), and during the process transfers heat to the gas that is entering the reaction region 12. The scroll heating device 1, therefore, has both heat transmitting and heat retaining abilities. The preheating design of the heating device makes it possible to convert chemical energy stably into thermal energy and provide the Stirling engine 9, which works at atmospheric pressure, with a heat source that generates heat steadily through lean combustion.

(25) In an experiment in which DME, methane, and syngas were used as the fuel gases, the scroll heating device 1 could drive the Stirling engine 9 to output electricity stably at 16 W when the base 11 was 3 mm thick, 10 W when the base 11 was 10 mm thick, and 6 W when the base 11 was 15 mm thick.

(26) In addition, the heating device of the present invention includes activated aluminum oxide balls (which serve as a catalyst carrier) placed in the first and the second channels 13 and 14. The activated aluminum oxide balls are wet-plated with a platinum salt (as a catalyst) and calcinated on the surface so as to reduce the activation energy required for reactions, allowing low-temperature oxidation/reduction to take place continuously in the heating device. The catalyst is added with cerium(IV) oxide to increase the oxygen-carrying ability of the catalyst. As an oxygen ion-conducting oxide, cerium(IV) oxide can easily form cerium(III) oxide by releasing the oxygen atoms in the lattice to form oxygen vacancies, thus contributing to the completeness of reaction, enhancing the activity of the catalyst, encouraging a mixed gas of fuel and air to react completely in the heating device, and retaining heat to maintain the temperature of the scroll heating device 1.

(27) Table 1 below shows the fuel equivalence ratios and thermoelectric conversion efficiencies of using DME, methane, and syngas for electricity output. As can be seen in the experiment data, DME is the fuel that had the highest combustion efficiency of 1.5%, and this is because DME has the highest energy density per unit volume and has similar properties to liquefied petroleum gas. DME can be pressurized at room temperature into a liquid state to facilitate transportation and storage, and is nowadays not only a notable alternative fuel for diesel engines, but also a substitute for liquefied petroleum gas for domestic use.

(28) TABLE-US-00001 TABLE 1 Fuel DME Methane Syngas Fuel equivalence ratio 0.375 0.794 0.383 Thermoelectric conversion efficiency (%) 1.50 1.10 1.18

(29) Thermal efficiency (η.sub.th) was calculated by the second, using the following equation:

(30) ${\eta }_{\mathrm{th}}=\frac{W_{\mathrm{out}}}{Q_{\mathrm{in}}}\{\begin{array}{c}{W}_{\mathrm{out}}:\mathrm{work}\mathrm{generated}\left(\mathrm{the}\mathrm{electricity}\mathrm{output}\mathrm{from}\mathrm{the}\mathrm{Stirling}\mathrm{engine}\right)\\ Q_{\mathrm{in}}:\mathrm{total}\mathrm{energy}\mathrm{of}\mathrm{the}\mathrm{fuel}\end{array}.$

(31) FIG. 7 shows the experiment result of using the Stirling engine 9 together with the scroll heating device 1 to output electricity, with the scroll heating device 1 coupled to the heating end of the Stirling engine 9 during the experiment. As can be known from the experiment result, the greater the temperature difference between the Stirling engine 9 and the scroll heating device 1, the greater the output power. The output power was about 12 W when the temperature difference was 200° C. The experiment result has shown that the scroll heating device 1 can be effectively coupled to the heating end of the Stirling engine 9 to increase heat transfer efficiency and thereby improve the performance of the Stirling engine 9 significantly.

(32) The present invention can be used with various low-heat-value fuels. For example, the readily available biogas generated from pig farm wastes can be used to output energy by way of the invention. The biogas produced during the pig raising process is composed essentially of methane, and as demonstrated by the experiment mentioned above, in which methane was used as one of the fuel gases of the scroll heating device 1, the use of the methane-containing pig-farm biogas can help reduce the emission of greenhouse gases effectively. Pig farmers can use the electricity generated by the device of the invention to power the electrical appliances on the farm, without having to rely on the power supplied by an electrical grid; that is to say, the farmers will be able to generate electricity locally and therefore gain the advantage of self-sufficient power generation. Besides, power generation in a distributed manner can prevent energy loss attributable to long-distance electricity transmission, thereby reducing unnecessary loss of energy.

(33) According to the above, the base 11, the reaction region 12, the first channel 13, the second channel 14, the pin fins 15, and the cover 16 of the scroll heating device 1 of the present invention are so configured and arranged that the first and the second channels 13 and 14 gradually narrow toward their respective outer ends and gradually widen toward their respective inner ends; that a gas moving through the first channel 13 to the reaction region 12 can be preheated by the exhaust in the immediately adjacent turns of the second channel 14 that flank the first channel 13; that the first channel 13, which gradually narrows toward its outer end and gradually widens toward its inner end, allows a gas flowing into the first channel 13 to flow toward the reaction region 12 at a progressively slower rate and then enter the reaction region 12 slowly through the gradually widening first channel 13, thereby increasing the duration of the combustion reaction of the gas; and that the portion of the exhaust that has just left the reaction region 12 and is moving through the second channel 14 toward the gas outlet 114 can preheat the portion of the ingoing gas that is about to enter the reaction region 12. The scroll heating device 1 not only transmits but also retains heat, and can reduce unnecessary heat dissipation and exergy destruction, allowing chemical energy to be converted into thermal energy stably. Also, the scroll heating device 1 has no limitation on the type of the fuel gas used, meaning the scroll heating device 1 can work with, and thereby remove the limitations conventionally imposed on, low-heat-value gases that are difficult to burn directly, making it possible to reuse energy effectively. Thus, the aforesaid objectives of the invention are achieved.

(34) While the invention has been described in connection with what is considered the most practical and preferred embodiments, it is understood that this invention is not limited to the disclosed embodiments but is intended to cover various arrangements included within the spirit and scope of the broadest interpretation so as to encompass all such modifications and equivalent arrangements.