Patent Application
20100212345
1. Field of the Invention
The present invention relates to a dehumidifying cooling device for district heating, and more particularly, to a dehumidifying cooling device for district heating which can perform an air cooling operation using hot water supplied by large-scale or small-scale district heating systems and gas-fired or oil-fired boilers installed in individual households.
2. Description of the Related Prior Art
There is a developing prospect that the recent high oil prices are not a temporary problem, but will be continuously maintained and fixed. Therefore, the main energy consuming countries of the world will increasingly make great efforts to secure stable energy resources. With the effectuation of the Tokyo protocol dealing with reduction in the discharge of greenhouse gas for the sake of preventing global warming, it will be expected that the international pressure for the limitation of fossil energy use, the criterion of energy efficiency, etc., will be strengthened.
According to a published energy report, the amount of energy consumed in domestic and business fields of Korea in 2003 was approximately 55 millions TOE, and was 25.2% of the total national energy consumption. This rate also corresponds to 41.9% on the basis of electricity use. For the past four years, the energy consumption of domestic and business fields shows an average annual rate of increase of 5.3%, whereas the consumption of electricity shows an average annual rate of increase of 12%. Accordingly, it will be appreciated that the consumption of electricity particularly has experienced a rapid increase. Estimating on the basis of variance in the monthly energy consumption of residential buildings and sample survey results about non-residential buildings as the subject of energy management, it is analyzed that 50% of the energy consumption of residential buildings and 47% of the energy consumption of business buildings are used for air conditioning. In conclusion, of the energy consumption of buildings, energy required for air conditioning occupies 13% of the national total energy consumption of Korea.
Accordingly, to guarantee the efficient use of energy and the continuous development of the energy industry while observing related international agreements, it is necessary to improve the efficiency of energy use for air conditioning in domestic and business fields. From this viewpoint, there is created a so-called collective-energy industry in which thermal energy and electricity, generated by facilities concentrated in a specific place for improving the efficiency of energy in domestic and business fields, are supplied collectively to multiple users in residential and business areas. It is reported that the collective-energy industry uses waste heat created during power generation as a heating source for space heating and hot water heating, thereby achieving not only a reduction of energy by approximately 20 to 30% by virtue of improved efficiency, but also an improvement of air environment by approximately 30 to 40% by virtue of a reduction of fuel usage and intensive environmental management. The collective-energy industry is evaluated as an effective industry, capable of dealing with related international environmental restrictions including climatic change conventions, etc. In the affirmative evaluation's debt, approximately 1.2 million families in Korea shared in the benefits of district heating in 2003, and in particular, 85% of supplied energy was generated by combined heat and power generation. Korea has a plan to expand the propagation of district heating to 2 million families by 2010.
In combined heat and power generation, called cogeneration, the generation ratio of electricity to heat is fixed at 3:5. Therefore, it is important to keep the ratio of electricity to heat at an appropriate level for maximizing the effect of the collective-energy industry. In Korea, the above mentioned generation ratio can be fulfilled in winter, but summer in Korea produces an increased electrical load for air cooling, and substantially no heat load. As a result, the operation rate of dedicatrd heating in summer decreases to less than 10%, and this causes deterioration in the economic efficiency of cogeneration. Actually, no generation results were reported between June and September in 2003.
To improve the operation rate of collective-energy generation facilities for efficiently using the effects of the industry, reducing the demand of heat in summer is necessary, and in particular, development and propagation of a technology for supplying cooling energy using distinct heating facilities is necessary.
In one example of the above described cooling energy supply technology, an absorption chiller is installed in a receptor, such as a large-scale building, etc., such that the chiller performs a central cooling operation using energy delivered from distinct heating facilities.
The absorption chiller is designed to chill water flowing in a pipe, using heat generated during the evaporation of a liquid-phase refrigerant, and condense the evaporated gas-phase refrigerant for reuse.
However, in spite of various researches and developments for improving the performance of the absorption chiller, there is a limit on the improvement of performance due to the low temperature of a heating source. In addition, the absorption chiller has an uneconomical high water return temperature because it cannot use water having a temperature of 80° C. or less, and suffers from a small differential between the temperature of supplied water and the temperature of returned water.
When the absorption chiller is installed in an apartment, etc. taking up the largest portion of district heating to provide central cooling, there is a problem in that cold water pipes have to be additionally installed regardless of hot water supply pipes.
The present invention has been made in view of the above problems, and it is an object of the present invention to provide a dehumidifying cooling device for district heating which can provide an air cooling operation by use of hot water supplied by large-scale or small-scale district heating systems and gas-fired or oil-fired boilers installed in individual households, thereby achieving a reduced device size via the implementation of an operation within the normal atmospheric pressure, and low manufacturing costs by virtue of a simplified system configuration.
In accordance with an aspect of the present invention, the above and other objects can be accomplished by the provision of a dehumidifying cooling device for district heating comprising: a case having a partition dividing the interior of the case into a wet channel and a dry channel, the wet channel having at one end, an outside air suction hole for introducing outside air into the wet channel and at the other end, an exhaust hole for discharging the outside air, the dry channel having at one end, a circulated air suction hole for introducing circulated air from a conditioning space into the dry channel and at the other end; an air supply hole for supplying cooling air into the conditioning space; a sensible heat exchanger configured to rotate through the plane of the partition and to heat exchange the outside air introduced into the wet channel through the outside air suction hole with the circulated air introduced into the dry channel; a heating coil installed in the wet channel between the back end of the sensible heat exchanger and the exhaust hole, and raising the temperature of the outside air passing through the wet channel by use of hot water introduced into the heating coil; a dehumidifying wheel configured to rotate through the plane of the partition behind the heating coil, adsorbing and removing moisture contained in the circulated air within the dry channel, the dehumidifying wheel being regenerated by evaporation of the adsorbed moisture to into the high-temperature outside air in the wet channel; and a regenerative-evaporative cooler installed in the dry channel between the circulated air supply hole and the sensible heat exchanger cooling the circulated air in the dry channel, which was dehumidified to high-temperature dry air by the dehumidifying wheel and subsequently heat exchanged and cooled by the sensible heat exchanger, the cooled circulated air being delivered to the air supply hole of the case.
Preferably, the device further comprises: a direct-evaporative cooler installed in the dry channel in front of the regenerative-evaporative cooler, the direct-evaporative cooler carrying out a secondary cooling operation of the circulated air discharged from the regenerative-evaporative cooler.
Preferably, the device further comprises: a first filter installed between the outside air suction hole and the sensible heat exchanger and removing impurities contained in the outside air; and an exhaust blower installed between the dehumidifying wheel and the exhaust hole and forcibly discharging the outside air from the wet channel through the exhaust hole. The first filter and the exhaust blower are installed in the wet channel.
Preferably, the device further comprises: a second filter installed between the circulated air suction hole and the dehumidifying wheel and removing impurities contained in the circulated air; and an air supply blower installed between the dehumidifying wheel and the sensible heat exchanger and forcibly discharging the cooled circulated air from the dry channel through the air supply hole. The second filter and the air supply blower are installed in the dry channel.
Preferably, the case is further provided with a cooler exhaust hole for discharging high-temperature air generated when the regenerative-evaporative cooler conducts secondary cooling operations.
Preferably, the amount of the high-temperature air to be discharged through the cooler exhaust hole is 30% of the total circulated air.
Preferably, the hot water to be introduced into the heating coil is delivered from any one of: a cogeneration plant, a heating boiler, a micro-turbine, a small gas engine, a small gas turbine, a gas-fired boiler, or an oil-fired boiler.
Preferably, the circulated air suctioned through the circulated air suction hole is mixed with the outside air at a predetermined mixing ratio of 7:3.
According to a dehumidifying cooling device for district heating of the present invention having the above described configuration, it is possible to provide air cooling by use of hot water supplied by large-scale or small-scale district heating systems and gas or oil boilers installed in individual households. Accordingly, the present invention has the effect of achieving a reduced device size through the implementation of the cooling operation without a compressor, and reduced manufacturing costs by virtue of a simplified system configuration.
The above and other objects, features and other advantages of the present invention will be more clearly understood from the following detailed description taken in conjunction with the accompanying drawings, in which:
The configuration of a dehumidifying cooling device for district heating according to the present invention will be described in detail with reference to the accompanying drawings.
In the following description of the present invention, a detailed description of known functions and configurations incorporated herein will be omitted, when inclusion of them may make the subject matter of the present invention rather unclear. Also, the terms used in the following description are defined taking into consideration the functions obtained in accordance with the present invention. The definitions of these terms should be determined based on the whole content of this specification because they may be changed in accordance with the option of a user or operator or a usual practice.
Referring to
The case 110 is made of metal and has a rectangular box shape. The case 110 is installed with a partition 119 dividing the interior of the case 110 into a wet channel 111 and a dry channel 115. The case 110 has an outside air suction hole 113 at one end of the wet channel 111 for introducing outside air into the wet channel 111, and an exhaust hole 112 at the other end of the wet channel 111 for discharging the outside air. The case 110 also has a circulated air suction hole 116 at one end of the dry channel 115, for introducing circulated air from a conditioning space CS into the dry channel 115, and an air supply hole 117 at the other end of the dry channel 115 for supplying cooling air into the conditioning space CS. The dry channel 115 of the case 110 is further provided with a cooler exhaust hole 118 for discharging high-temperature air generated while the regenerative-evaporative cooler 190 carries out a secondary cooling operation that will be described hereinafter. The circulated air, introduced into the case 110 through the circulated air suction hole 116, is mixed with the outside air at a ratio of 7:3, to keep the interior of the case 110 in the atmospheric pressure state.
The first filter 120 is located in the wet channel 111 of the case 110 between the outside air suction hole 113 and the sensible heat exchanger 130. The first filter 120 is used to remove impurities and odors from the suctioned outside air. Preferably, the first filter 120 is an antibacterial filter, and is easily separable from the case 110.
The sensible heat exchanger 130 has a rotating shaft 131 installed in the plane of the partition 119 and takes the form of a disc rotating on shaft 131 inside the wet channel 111 and the dry channel 115 of the case 110. The sensible heat exchanger 130 is used to heat exchange the outside air introduced into the wet channel 111 through the outside air suction hole 113 with the circulated air introduced into the dry channel 115. The sensible heat exchanger 130 is a honeycomb-patterned disc fabricated by processing a thin plate, such as an aluminum plate, etc. The sensible heat exchanger 130 carries out a primary heat exchange operation for lowering the temperature of the circulated air that is dehumidified by passing through the dehumidifying wheel 150 to be described hereinafter. There are a motor and belt (not shown) for rotation of the sensible heat exchanger 130.
The heating coil 140 is located in the wet channel 111 of the case 110 between a back end of the sensible heat exchanger 130 and the exhaust hole 112. The heating coil 140 raises the temperature of the outside air passing through the wet channel 111 by use of hot water introduced therein. The hot water introduced into the heating coil 140 is delivered from any one of: a cogeneration plant, a heating boiler, a micro-turbine, a small gas engine, a small gas turbine, a gas-fired boiler, or an oil-fired boiler, and has a temperature within a range of 60 to 120° C.
The dehumidifying wheel 150 has a rotating shaft 151 installed in the plane of partition 119, and takes the form of a disc to rotating on shaft 151 inside the wet channel 111 and the dry channel 115 of the case 110. The dehumidifying wheel 150 is located behind the heating coil 140 and serves to adsorb and remove moisture contained in the circulated air within the dry channel 115. The dehumidifying wheel 150 is regenerated by evaporating the adsorbed moisture to thereby supply the moisture into the high-temperature outside air within the wet channel 111. The dehumidifying wheel 150 is a honeycomb-patterned disc containing an adsorbent, such as silica gel, zeolite, or the like, for adsorbing the moisture contained in the circulated air in a dry adsorption manner. There are a motor and belt (not shown) for rotation of the dehumidifying wheel 150.
The exhaust blower 160 is installed in the wet channel 111 of the case 110 between the dehumidifying wheel 150 and the exhaust hole 112, and forcibly discharges the outside air from the wet channel 111.
The second filter 170 is installed in the dry channel 115 of the case 110 between the circulated air suction hole 116 and the dehumidifying wheel 150 and removes impurities and odors from the circulated air. Preferably, the second filter 170 is an antibacterial filter, and is easily separable from the case 110.
The air supply blower 180 is installed in the dry channel 115 of the case 110 in front of the dehumidifying wheel 150 and forcibly discharges the circulated air from the dry channel 115 through the circulated air supply hole 117.
The regenerative-evaporative cooler 190 is installed in the dry channel 115 between the circulated air supply hole 117 and the sensible heat exchanger 130. After the circulated air introduced into the dry channel 115 is dehumidified by the dehumidifying wheel 150 so as to be changed to high-temperature dry air, and subsequently heat exchanged and cooled by the sensible heat exchanger 130, the regenerative-evaporative cooler 190 further cools the circulated air. The cooled circulated air is delivered to the air supply hole 117 of the case 110, while the high-temperature air generated during cooling is delivered to the cooler exhaust hole 118. The amount of the high-temperature air to be discharged through the cooler exhaust hole 118 is 30% of the total circulated air. The interior of the regenerative-evaporative cooler 190 is divided into a dry channel and a wet channel. If a part of the air passing through the dry channel is delivered into the wet channel, the air is cooled as water is evaporated by the high-temperature surface of the wet channel, which acts to absorb heat from the remaining higher temperature air passing through the dry channel. The air passing through the dry channel can be cooled to a dew-point temperature to the maximum extent without an increase of humidity. The configuration of the regenerative-evaporative cooler 190 is disclosed in Korea Patent Registration No. 0409265 and thus, a detailed description thereof will be omitted herein.
The direct-evaporative cooler 200 is installed in the dry channel 115 of the case 110 in front of the regenerative-evaporative cooler 190. The direct-evaporative cooler 200 serves to carry out a secondary cooling operation of the circulated air from the regenerative-evaporative cooler 190, so as to supply the resulting air into the conditioning space CS through the air supply hole 117 of the case 110.
Hereinafter, the operation and effects of the dehumidifying cooling device for district heating according to the present invention will be described in detail with reference to
First, explaining a dehumidifying cooling operation carried out in the dry channel 115, circulated air from the conditioning space CS, which is mixed with high-temperature and high-humidity outside air, is introduced into the dry channel 115 of the case 110 through the circulated air suction hole 116 by the air supply blower 180. After passing through the second filter 170, the introduced circulated air subsequently passes through the dehumidifying wheel 150 such that the moisture contained in the circulated air is removed by the adsorbent.
The dehumidified circulated air is heated by adsorptive heat generated from the surface of the dehumidifying wheel 150. The resulting high-temperature and low-humidity circulated air is heat exchanged with the outside air in the wet channel 111 by the sensible heat exchanger 130. Thus, the circulated air is changed to the low-temperature air prior to being introduced into the regenerative-evaporative cooler 190.
When the circulated air is introduced into the regenerative-evaporative cooler 190, 70% of the circulated air is cooled while passing through the regenerative-evaporative cooler 190, and 30% of the circulated air is discharged to the outside through the cooler exhaust hole 118.
The circulated air, having passed through the regenerative-evaporative cooler 190, is secondarily cooled while passing through the direct-evaporative cooler 200, then is supplied into the conditioning space CS through the air supply hole 117 of the case 110.
Next, explaining a heat-exchange operation carried out in the wet channel 111, high-temperature and high-humidity outside air is introduced into the wet channel 111 through the outside air suction hole 113 and passes through the first filter 120 under the operation of the exhaust blower 160. Then the filtered outside air is heat exchanged with the circulated air in the dry channel 115 by the sensible heat exchanger 130, such that the temperature of the outside air is raised. Then the outside air with the raised temperature passes through the heating coil 140.
While passing through the heating coil 140, the temperature of the outside air is further raised by hot water supplied to the heating coil 140. Thus, the outside air to be delivered into the dehumidifying wheel 150 has a significantly raised temperature.
As the dehumidifying wheel 150 rotates in a state of adsorbing moisture, the outside air forcibly evaporates moisture while passing through the dehumidifying wheel 150, and thereafter, is discharged to the outside through the exhaust hole 112. Through the above described process, the surface of the dehumidifying wheel 150 is returned to an original dried state, thereby recovering its dehumidifying ability.
Referring to
Then, the air {circle around (3)} is heat exchanged with outside air {circle around (8)} in the wet channel while passing through the sensible heat exchanger such that the heat exchanged air {circle around (4)} has a slightly lowered temperature. In sequence, while passing through the regenerative-evaporative cooler, the temperature of the air {circle around (4)} is rapidly lowered to produce significantly cooled air {circle around (5)}. Thereafter, while passing through the direct-evaporative cooler, the temperature of the air {circle around (5)} is further lowered slightly, but the absolute humidity of the air {circle around (5)} is raised, thereby resulting in cooling air {circle around (6)}.
Meanwhile, when the introduced outside air {circle around (7)} passes through the first filter, the filtered air {circle around (8)} has the same temperature and absolute humidity as does the outside air {circle around (7)}. The filtered air {circle around (8)} is heat exchanged with the circulated air {circle around (3)} in the dry channel while passing through the sensible heat exchanger. The resulting heat exchanged air {circle around (9)} is slightly raised in temperature, but keeps the same absolute humidity as that of the air {circle around (8)}. Then, the temperature of the air {circle around (9)} is rapidly raised while passing through the heating coil, resulting in high-temperature air {circle around (10)}.
The high temperature air {circle around (10)} is lowered in temperature but raised in absolute humidity in the course of passing through the dehumidifying wheel, thereby being changed to low-temperature and high-humidity air {circle around (11)}.
In conclusion, in the dehumidifying cooling device for district heating according to the present invention, air to be supplied into a conditioning indoor space is subjected to the transfer of heat and moisture via a direct contact with the dehumidifying cooling device. This has the effect of achieving excellent transfer efficiency and producing and supplying cooling air with a low-temperature heating source of 60° C. Further, differently from conventional absorptive devices, the dehumidifying cooling device is operable in normal atmospheric pressure and has a simplified configuration, resulting in a considerable reduction of manufacturing costs.
As apparent from the above description, a dehumidifying cooling device according to the present invention can be installed in residential and business buildings, etc. using hot water delivered from district heating facilities as a source for cooling a room.
Although the preferred embodiments of the present invention have been disclosed for illustrative purposes, those skilled in the art will appreciate that various modifications, additions and substitutions are possible, without departing from the scope and spirit of the invention as disclosed in the accompanying claims.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10-2007-0010671 | Feb 2007 | KR | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/KR2007/001147 | 3/8/2007 | WO | 00 | 2/4/2008 |
