Experimental Research of Shell and Tube Condenser With the Middle Liquid Separation Structure

Author(s):  
Kai Zhu

For the state of condensation in tube, liquid condensate separation in middle process can prolong the state of steam entrance region of higher heat transfer coefficient. It is called short-tube effect theory. Combined with the traditional condenser, a shell and tube condenser was designed for experiment research in this paper, and compared with the traditional condenser by opening liquid distribution pipes arranged in both sides of condenser. The results showed that liquid distribution pipes with different diameter have different condensation effect. Under the same steam flow rate of inlet, liquid distribution pipes with different combination of diameter and number indicated that its coefficient of heat transfer are higher than the traditional heat transfer by 14.2%, 15.5% and 25.1%. This result illustrated that heat exchange efficiency of a shell and tube condenser with liquid distribution pipes is better than a traditional condenser.

2017 ◽  
Vol 19 ◽  
pp. 38-47 ◽  
Author(s):  
Adebola S. Kasumu ◽  
Nashaat N. Nassar ◽  
Anil K. Mehrotra

Author(s):  
Yingying Yao ◽  
Jinfeng Zhao ◽  
Shouheng Sun ◽  
Hang Wang ◽  
Shan Yang ◽  
...  

Author(s):  
C. V. Le ◽  
P. K. Bansal ◽  
J. D. Tedford

This paper presents a system simulation model of an oil-injected screw liquid chiller, where the refrigerant shell and tube heat exchangers are modelled following local heat transfer integration approach. All major components of the system are modelled in a modular format such as an oil-injected screw compressor, a shell and tube condenser, a flooded evaporator, and a high side-float valve. The simulation results are validated with the experimental data of a multiple-chiller plant at a process industry. The validated results show that the part-load ratio and the glycol-water temperature at the evaporator inlet affect the system performance considerably as compared to the temperature of cooling water entering the condenser.


2015 ◽  
Vol 55 (5) ◽  
pp. 306 ◽  
Author(s):  
Jan Havlík ◽  
Tomáš Dlouhý

<p>This paper presents an analysis of heat transfer in the process of condensation of water vapor in a vertical shell-and-tube condenser. We analyze the use of the Nusselt model for calculating the condensation heat transfer coefficient (HTC) inside a vertical tube and the Kern, Bell-Delaware and Stream-flow analysis methods for calculating the shell-side HTC from tubes to cooling water. These methods are experimentally verified for a specific condenser of waste process vapor containing air. The operating conditions of the condenser may be different from the assumptions adopted in the basic Nusselt theory. Modifications to the Nusselt condensation model are theoretically analyzed.</p>


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