Patent Application
20100243209
The present invention relates to a single pipe collector for a heat pump installation. The present invention also relates to heat pump system comprising the single pipe collector.
In water, ground and down in the bedrock, there are a heat source free of cost. Use of heat from sea, surface ground heat and bedrock heat is a secure, safe and environmental heating technique. The heat energy can be transmitted to an existing, conventional waterborne heating system and also used for hot-water production.
In a geothermal heating system, the hear is extracted from a bore hole, a so called drilled energy well. The collector is the pipe, which comprises a heat transfer medium in the form of a so called heat transfer liquid, that convey heat through the heated heat transfer medium and that also convey the cooled heat transfer medium back in a closed cycle.
In a surface ground heat plant, a several hundred meter long tubing is buried to a frostproof depth and arranged in coils. The collector tubing collects the heat that occur in the ground and use it to vaporize the cooling agent of the heat pump.
Sea heat works fundamentally in the same way as surface ground heat. The energy that exists stored in the sea water and in bottom layer is utilized. The collector tubing is put on the bottom of a water course.
There are various kinds of heat pump collectors. The kind of collector, that is the most frequent today, is called U-pipe collector. According to that principle, a separate, closed pipe is arranged in a drilled hole. This is for example carried out such that a continuous elongated pipe of plastics, suitably polyethylene, is bent on the middle such that it forms a U-shape. The lowest part of the “U” of the pipe is arranged on the drilled hole, and subsequently the pipe is advanced down into the drilled hole. Thus, the U-pipe forms a single continuous line for the heat transfer liquid in a closed cycle, in direction from the heat pump down into to drilled hole and back out of the drilled hole and further back to the heat pump in the one and the same pipe.
For installations of geothermal heating there are also a so called three-pipe collector, which is a variant of a collector that comprises a pipe for conveyance of the heat transfer liquid down into the drilled hole, which pipe has a branching-off to two pipes that transports the heat transfer liquid back from the drilled hole and further to heat pump. The term “single pipe collector” in this disclosure is a common term for the coils of collectors and collector tubing mentioned above that are intended for sea heat and surface ground heat. In the single pipe collector, the heat transfer liquid can be lead in a pipe with essentially the same cross-sectional area along the whole longitudinal extension of the collector.
Another type of collector according to the prior art is the so called coaxial collector. An inner pipe is arranged in an outer pipe. The pipes are welded together to one unit that subsequently is installed in a drilled hole. The purpose with this technique, having “a pipe in a pipe” is that it is desirable to avoid mixing for too long time of the cooled heat transfer liquid, that is brought down into the bore hole, with the heated heat transfer liquid, that shall be carried up in the collector. By providing an outer pipe with large diameter, a slower flow in the outer pipe having large diameter is achieved, whereby a positive output is reached when it comes to heat absorption quality. The coaxial collector is not found in any considerable extent on the market today, since this technique involves large installation and production costs. However, the coaxial collector is generally considered to be more effective than the conventional single pipe collector.
DE 20 2004 007 567 U1 discloses a coaxial collector according to the well known kind, described above. This comprises a connecting pipe for inflow of heat transfer liquid to an outer pipe, that comprises an uneven surface structure on the inside of the outer pipe. The heated heat transfer liquid is returned via an inner pipe up through a connecting pipe.
US 2007/0023163 A1 discloses a coaxial collector according to the well known kind as described above. This comprises a connecting pipe for inflow of heat transfer liquid in an inner pipe, that ends just above the bottom of an outer pipe, arranged outside the inner pipe. The heat transfer liquid is heated during circulation in the space between the outer pipe and the inner pipe, while guided via a helical structure (“turbulence generator” or turbulence generating structure”) arranged on the outside of the inner pipe and further conveyed to a heat exchanger via a pump.
The wall thickness on the collector pipe is optimized such that the heat transfer medium obtain a maximal absorption of heat, the pipes becomes easy to handle and such that the return weight strive straight down into the bore hole, in the case with a drilled energy well. The length is adapted as desired.
However, a problem with the traditional single pipe collector is that the absorption of energy from the surrounding water in the energy well is not optimal. There is a large need for a more effective utilization of the energy. This also applies to the single pipe collectors that are intended for sea systems and surface ground heat plants.
It is an object with the present invention to at least partially eliminate those drawbacks that are associated with apparatuses according to the state of the art. Further, one object is to achieve an improved absorption of energy for the heat transfer medium in a single pipe collector from the surrounding ground in a surface ground heat plant, or from the surrounding water in an energy well for a geothermal heating system or in a sea heating system.
This object has been reached with a single pipe collector for a heat pump installation according to the present invention. The collector comprises a pipe intended for installation in a heat pump system, in which pipe a heat transfer liquid circulates in a closed cycle for conveyance of heat that is absorbed from a heat source to a heat pump and return of the heat transfer liquid back to the heat source. The inward surface of the pipe has an uneven surface structure that comprises indentations and/or elevations.
By the single pipe collector, and a heat pump plant comprising the single pipe collector, according to the present invention, an improved absorption of energy is accomplished since the uneven surface structure creates a turbulent flow, in comparison to collectors according to the prior art for sea heat, surface ground heat plant or energy wells, which have a smooth inward surface that provides a laminar flow of the heat transfer medium through the collector.
By the term “pipe” in this description, is also meant hose, conduit, or the like.
According to one embodiment, the surface structure on the inward surface is a grooved pattern, whereby the surface is designed with indentations that suitably forms continuous recesses in the surface that extends essentially in the longitudinal direction of the pipe. The recesses may be evenly spread around the inner circumferential surface of the pipe, as seen in a cross-section of the pipe.
According to another embodiment, the indentations and/or elevations extends helically in the longitudinal direction of the pipe. The direction of the helical shape can be altered at least at some portion in the longitudinal direction of the pipe, suitably at least every two meters, preferably each meter, in the longitudinal direction of the pipe.
Additional preferred features, advantages and favourable embodiments of the invention, are evident from the dependent claims, and also in the following from description of the embodiments.
The present invention will now be described more in detail by examples of application, by reference to the accompanying drawings, without limiting the interpretation of the invention thereto, where
A part of the single pipe collector for a geothermal heating system, according to an embodiment of the present invention, is shown in
According to a preferred embodiment, the single pipe collector according to the present invention is a continuous pipe 12 with a cross-sectional area that is essentially similar along the whole longitudinal direction L of the pipe.
According to a preferred embodiment, the surface structure on the inward surface 14 of the single pipe collector is a grooved pattern, whereby the inward surface is designed with indentations 18 that suitably forms continuous grooves in the surface that extends essentially in the longitudinal direction L of the pipe. The grooves are evenly spread around the inner circumferential surface of the pipe, as seen in a cross-section T of the pipe.
According to the present invention, the grooves or the pattern, such as a surface structure of indentations and/or elevations, may be continuous or discontinuous in the longitudinal direction of the single pipe collector. As shown in the embodiment in
Usual dimensions for the collector pipes 12 according to the invention are within the range 25-63 mm in diameter. The height of the indentations and/or elevations 16, alternatively the grooves 18 or the grooving, can be varied, but can typically be within the range of 0.2-5 mm depending on the size of the pipes and the wall thickness, preferably 0.2-2 mm, for the most usual dimensions of the collector pipes 12.
Experiments were carried out in a heat pump system, with two heat pumps of 16 kW and 32 kW, respectively, for supply of hot water and heating in a building with 19 apartments each with an area of 40 m2. Four of the water filled bore holes, with a diameter of 140 mm and a depth of 260 mm, that constitutes the heat source of the system, were used in the experiment. Ethanol in a concentration of 20 percentage by volume in an aqueous solution, with a freezing point of −8° C. In the experiment, each of the four boreholes was equipped with four different types of single pipe collectors, respectively. The respective borehole design, dimension and arrangement are tabulated in. Table 1 below.
The mean undisturbed ground temperature was measured to 8.7° C., and the average ground thermal conductivity 3,75 W/m K. It should also be explained that single pipe collector no. 2 (BH2) in the Table, that is the three-pipe collector, is a variant of collector that comprises one pipe for conveyance of the heat transfer liquid down into the bore hole and two pipes that guides the heat transfer liquid back out of the bore hole and further to a heat pump. The single pipe collector no. 4 (BH4) is a conventional U-pipe collector. The single pipe collector no. 5 (BH5) is a conventional U-pipe collector provided with spacers, that are intended to keep the pipes apart in the bore hole such that they not will be in contact with each other. The single pipe collector no. 6 (BH6) is a U-pipe collector according to the present invention, that comprises indentations and/or elevations on the inward surface of the pipe in a helical extension along the longitudinal extension of the pipe. The helical shape is altered periodically along the longitudinal extension of the pipe.
The flows in the respective collectors were checked. Each borehole heat exchanger was instrumented with thermocouples for temperature measurements at the bottom and outlet points, on the heat transfer liquid inwards of the collector. The total pressure drop in the collectors is also measured during the tests at the collector inlet and outlet lines using a pressure gauge. Temperatures have been measured at different flow conditions in the bore holes and when the conditions have stabilized after the heat pump start up. During a measuring period the fluid density, kinematic viscosity and heat capacity were calculated at the measured temperature. Hence, the Reynolds number, the friction factor and the pressure drop were calculated. Finally, the heat absorbed per meter by the heat transfer fluid was calculated for each collector, which was used in order to calculate the borehole thermal resistance for each of the collector as well. The temperature value for the borehole wall was measured by the aid of a fibre optical cable and was assumed to be constant and equal to 7.2° C. for the calculations in this experiment.
With respect to heat extraction (kW), the best heat extraction performance is obtained in BH6 and the worst performance is in BH2. Nevertheless, it is not recommended to compare the collectors by looking at the extracted heat due to the fact that not all the measurements were taken at the same time, which could cause different inlet and groundwater temperatures at different measurement occasions. With respect to the thermal resistance, it was observed that BH6 had the lowest values of all the collectors (e.g. at an up flow of 1.8 m3/h, BH6 had about 0.16 K/(W/m) while BH2 had about 0.18, BH4 had about 0.23 and BH5 had about 0.22), with the exception for one measured value where BH5 were best. Hence, this means for one aspect that the single pipe collector according to the invention shows the best performance. The result for the pressure drop is evident from Table II below.
To sum up, the results implies that the pipe dimensions have an important influence, the spacers (collector in BH5) contributes probably not to increased heat transmission and that a surface structure on the inside of the pipes improves the performance of the collectors. With the exception of BH6, it is generally observed that the calculated pressure drop is slightly lower than the experimental values. This is attributed to the fact that the accessories such as elbows, bends, bottom part of the collector, are not considered in the calculation. It is observed that the calculated values for BH6 are higher than the experimental ones, which unexpectedly shows that the real pressure drop in the single pipe collector with surface structure on its inward surface, in the shape of indentations and/or elevations according to the present invention, is in fact lower. BH6 has the lowest pressure drop of all the collectors of the BHEs, including BH4 and BH5 which are common U-pipe collectors with the same dimensions. This is surprising. The pressure drop analysis indicates that BH6 is the best option, since the required pumping power for the heat transfer fluid would be slightly lower for this collector.
| Number | Date | Country | Kind |
|---|---|---|---|
| 0702240-3 | Oct 2007 | SE | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/SE2008/051040 | 9/17/2008 | WO | 00 | 6/14/2010 |
