Heat Exchangers for Low Temperature Plants

1964 ◽  
Vol 67 (541) ◽  
pp. 202-210
Author(s):  
Teiji SATO
Energies ◽  
2019 ◽  
Vol 12 (10) ◽  
pp. 1853 ◽  
Author(s):  
Pavel Neuberger ◽  
Radomír Adamovský

The efficiency of a heat pump energy system is significantly influenced by its low-temperature heat source. This paper presents the results of operational monitoring, analysis and comparison of heat transfer fluid temperatures, outputs and extracted energies at the most widely used low temperature heat sources within 218 days of a heating period. The monitoring involved horizontal ground heat exchangers (HGHEs) of linear and Slinky type, vertical ground heat exchangers (VGHEs) with single and double U-tube exchanger as well as the ambient air. The results of the verification indicated that it was not possible to specify clearly the most advantageous low-temperature heat source that meets the requirements of the efficiency of the heat pump operation. The highest average heat transfer fluid temperatures were achieved at linear HGHE (8.13 ± 4.50 °C) and double U-tube VGHE (8.13 ± 3.12 °C). The highest average specific heat output 59.97 ± 41.80 W/m2 and specific energy extracted from the ground mass 2723.40 ± 1785.58 kJ/m2·day were recorded at single U-tube VGHE. The lowest thermal resistance value of 0.07 K·m2/W, specifying the efficiency of the heat transfer process between the ground mass and the heat transfer fluid, was monitored at linear HGHE. The use of ambient air as a low-temperature heat pump source was considered to be the least advantageous in terms of its temperature parameters.


Author(s):  
Benedikt Hoegel ◽  
Dirk Pons ◽  
Michael Gschwendtner ◽  
Alan Tucker ◽  
Mathieu Sellier

Low-temperature heat sources such as waste heat and geothermal energy in the range from 100 ℃ to 200 ℃ are widely available and their potential is largely untapped. Stirling engines are one possibility to convert this heat to a usable power output. Much work has been done to optimise Stirling engines for high-temperature heat sources such as external combustion or concentrated solar energy but only little is known about suitable engine layouts at lower temperature differences. With the reduced temperature difference, changes become necessary not only in the heat exchangers and the regenerator but also in the operating parameters such as frequency and phase angle. This paper shows results obtained from a third-order simulation model that help to identify beneficial parameter combinations, and explains the differences of low and high-temperature engines.


1983 ◽  
Vol 15 (10) ◽  
pp. 247-261
Author(s):  
Per Erik Sørås ◽  
Arve Thendrup ◽  
Svein Tryggestad

The cooling water discharge from the gas terminal at Kårstø in Norway will be in the order of 7 m3/s and heated about 10°C. The cooling water will be withdrawn through an intake structure at 25 m depth and discharged at 10 m depth. The intake structure and the intake depth were chosen in order to prevent recycling of cooling water, to withdraw water with a stable and low temperature and to prevent fouling in the heat exchangers. The analyzing methods and results will be presented. The outlet area consists of several small islands, sounds and fjords. Salinity and temperature were measured to determine the stratification. In order to calculate the volume exchange and hence the excess temperatures in the outlet area, a great number of current measurements with continously recording instruments were performed. Tracer measurements and drift card investigation were also performed in order to evaluate the transport and dilution of the cooling water discharge.


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