Effects of horizontal tube arrays on heat transfer in an external heat exchanger

2020 ◽  
Vol 181 ◽  
pp. 115964
Author(s):  
Runxia Cai ◽  
Boyu Deng ◽  
Xin Tao ◽  
Yi Zhang ◽  
Hairui Yang ◽  
...  
2013 ◽  
Vol 448-453 ◽  
pp. 3259-3269
Author(s):  
Zhi Wei Li ◽  
Hong Zhou He ◽  
Huang Huang Zhuang

The characteristics of the external heat exchanger (EHE) for a 4 MWth circulation fluidized bed combustor were studied in the present paper. The length, width and height of EHE were 1.5 m, 0.8 m and 9 m, respectively. The circulating ash flow passing the heating surface bed could be controlled by adjusting the fluidizing air flow and the heating transferred from the circulating ash to the cooling water. The ash flow rate passing through the heat transfer bed was from 0.4 to 2.2 kg/s. The ash average temperature was from 500 to 750 °C. And the heat transfer rate between the ash and the cooling water was between 150 and 300 W/(m2·°C). The relationships among the circulating ash temperature, the heat transfer, heat transfer rate, the heat transfer coefficient and the circulating ash flow passing through the heating exchange cell were also presented and could be used for further commercial EHE design.


Author(s):  
Amir Jokar ◽  
Mohammad H. Hosni ◽  
Steven J. Eckels

The thermal-fluid characteristics of an automotive radiator, used as the external heat exchanger in an auto air conditioning system, are experimentally analyzed and discussed in this article. The radiator in this study is a compact heat exchanger with parallel rectangular minichannels and louvered thin-plate fins. A 50% glycol-water mixture flows through the minichannels with staggered surface enhancements on the walls. On the other side, air flows through the radiator openings with the louvered thin-plate fins sandwiched between the minichannels. Single-phase heat transfer and pressure drop correlations for glycol-water flow within the minichannels and for air flow through the louvered fins are obtained and presented. The Wilson plot technique is applied to find the heat transfer coefficients on both the glycol-water and air sides. The frictional pressure drop for the glycol-water flow within the minichannels is also obtained using the Fanning equation. The uncertainty estimates for both measured and calculated parameters are then presented, and finally the results are plotted, discussed and compared with the relevant previous studies. These results show that the heat transfer rate is increased in the glycol-water side due to the surface enhancements in comparison with smooth rectangular channels. The heat transfer is enhanced on the air side as well, as compared with the flat smooth surfaces, due to the use of louvered fins.


Energies ◽  
2021 ◽  
Vol 14 (17) ◽  
pp. 5553
Author(s):  
Artur Blaszczuk ◽  
Szymon Jagodzik

In the research work, energy transport between a dense fluidized bed and submerged horizontal tube bundle is analyzed in the commercial external heat exchanger (EHE). In order to investigate the heat transfer behavior, the authors carried out eight performance tests in a fluidized bed heat exchange chamber with a cross-section of 2.7 × 2.3 m in depth and width and a height of 1.3 m. The authors have been developing a mechanistic model for the prediction of the average heat transfer coefficient, which includes the effect of the geometric structure of the tube bundle and the location of the heat transfer surface on the heat transfer rate. The computational results depict that the average heat transfer coefficient is essentially affected by superficial gas velocity and suspension density rather than bed particle size. The empirical correlations have been proposed for predicting heat transfer data since the existing literature data is not sufficient for industrial fluidized bed heat exchangers. On the basis of the evaluated operating conditions of an external heat exchanger, the optimal conditions where heat transfer occurs could be deduced. The developed mechanistic heat transfer model is validated by experimental data under the examined conditions.


2013 ◽  
Vol 732-733 ◽  
pp. 11-17
Author(s):  
Da Long Zhang ◽  
Ding Hua Yang ◽  
Gen Sheng Yang ◽  
Zhong Li ◽  
Jun Fu Lv

A heat transfer model of external heat exchanger (EHE) in large-scale circulating fluidized bed (CFB) boiler was suggested based on experiment data and theoretical analysis. And the model parameters were also provided. With this model, the heat transfer performance of the EHE in an actual operating 300MW CFB boiler was predicted. The comparison between the model predictive results and the actual results showed that the relative error is less than 7%. This indicated that the model established in this paper is reliable and can provide a significant reference in EHE of large-scale CFB boiler design.


1991 ◽  
Vol 28 (02) ◽  
pp. 73-83
Author(s):  
Roy H. Cottrell ◽  
Jack W. Hoyt

The refrigeration system in use aboard today's modern tuna seiners was developed in the late 1930's for use aboard bait boats. Since that time, fishing methods have changed, vessel carrying capacities have increased tenfold, catch rates have increased fivefold, and individual fishwell sizes have increased fourfold. As a result, although catch rates have 9one up, the refrigeration effect per ton of tuna per well has actually gone down. Despite these trends, the current refrigeration system works remarkably well. This is due partly to its inherent flexibility and partly to the durability of the tuna with respect to its intended canned market. Nevertheless, because of the increase in well sizes and catch rates, a small percentage of fish is currently being lost due to inadequate refrigeration. This results in an economic loss to the fishing fleet. These losses seem to occur when many fish are caught at a time and loaded into large fishwells. While part of the solution is operational changes, some of which have been recommended elsewhere [1], 3 it has been suggested that increasing the refrigeration effect per well will also help overcome problems observed in the present system. Of the many alternatives which could increase the refrigeration effect per well, this paper discusses the addition of an external heat exchanger, called a chiller, to augment the refrigeration effect per well provided by the existing coil evaporators lining the fishwell bulkheads. Available data on refrigeration effectiveness of modern tuna seiners are analyzed and a computer simulation of the system is presented. Other computer results deal with augmentation of the present system by the addition of additional refrigeration capacity through an external chiller. In addition, a new model for the heat transfer involved in freezing fish such as tuna is presented.


Author(s):  
A. V. Morozov ◽  
O. V. Remizov ◽  
A. A. Tsyganok

The experimental investigations of non-condensable gases effect on the steam condensation inside multirow horizontal tube bundle of heat exchanger under heat transfer to boiling water were carried out at the large-scale test facility in the Institute for Physics and Power Engineering (IPPE). The experiments were carried out for natural circulation conditions in primary and secondary circuits of the facility at primary circuit steam pressure of Ps1 = 0.34 MPa. The experimental heat exchanger’s tube bundle consists of 248 horizontal coiled tubes arranged in 62 rows. Each row consists of 4 stainless steel tubes of 16 mm in outer diameter, 1.5 mm in wall thickness and of 10.2 m in length. The experimental heat exchanger was equipped with more than 100 thermocouples enabling the temperatures of primary and secondary facility circuits to be controlled in both tube bundle and in the inter-tubular space. The non-condensable gases with different density — nitrogen and helium were used in the experiments. The volumetric content of gases in tube bundle amounted to ε = 0.49. The empirical correlation for the prediction of the relative heat transfer coefficient k/k0 = f (ε) for steam condensation in steam-gas mixture was obtained.


Sign in / Sign up

Export Citation Format

Share Document