scholarly journals Experimental study on thermal performance in three-flow cooling tower

2020 ◽  
Vol 329 ◽  
pp. 03007
Author(s):  
Ilnur Madyshev ◽  
Ildar Sabanaev ◽  
Vitaly Kharkov ◽  
Lenar Ganiev ◽  
Andrey Dmitriev

Biofouling can significantly deteriorate the efficiency of cooling towers. A cooling tower with a three-flow cooling circuit has been developed. The fill pack consists of inclined-corrugated contact elements with perforation. One of the advantages of the proposed cooling tower is the possibility of uniform distribution of liquid over the cross-sectional area. The paper represents the results of an experimental study of the thermal performance of the three-flow cooling tower. It was found that when the wetting rate of the liquid increases, the thermal performance of the cooling tower can reach 47.8%. The developed three-flow cooling tower allows excluding the propagation of microorganisms and reducing the biofouling of industrial water systems along with the high performance for circulating water.

Author(s):  
Mostafa H. Sharqawy ◽  
John H. Lienhard ◽  
Syed M. Zubair

Seawater cooling towers have been used since the 1970’s in power generation and other industries, so as to reduce the consumption of freshwater. The salts in seawater are known to create a number of operational problems including salt deposition, packing blockage, corrosion, and certain environmental impacts from salt drift and blowdown return. In addition, the salinity of seawater affects the thermophysical properties which govern the thermal performance of cooling towers, including vapor pressure, density, specific heat, viscosity, thermal conductivity and surface tension. In this paper, the thermal performance of seawater cooling towers is investigated using a detailed model of a counterflow wet cooling tower. The model takes into consideration the coupled heat and mass transfer processes and does not make any of the conventional Merkel approximations. In addition, the model incorporates the most up-to-date seawater properties in the literature. The model governing equations are solved numerically and its validity is checked by data in the literature. Based on the results of the model, a correction factor is obtained which characterizes the degradation of the cooling tower effectiveness when seawater is used.


2009 ◽  
Vol 13 (4) ◽  
pp. 91-98
Author(s):  
Elazm Abo ◽  
Farouk Elsafty

The main objective of this study is to find a proper solution for the cross-flow water cooling tower problem, also to find an empirical correlation's controlling heat and mass transfer coefficients as functions of inlet parameters to the tower. This is achieved by constructing an experimental rig and a computer program. The computer simulation solves the problem numerically. The apparatus used in this study comprises a cross-flow cooling tower. From the results obtained, the 'characteristic curve' of cross-flow cooling towers was constructed. This curve is very helpful for designers in order to find the actual value of the number of transfer units, if the values of inlet water temperature or inlet air wet bulb temperature are changed. Also an empirical correlation was conducted to obtain the required number of transfer units of the tower in hot water operation. Another correlation was found to obtain the effectiveness in the wet bulb operation.


Author(s):  
J. M. Burns ◽  
D. C. Burns ◽  
J. S. Burns

Section 316(b) of the Clean Water Act regulates the potential environmental impacts of cooling water intakes in order to mitigate the adverse entrainment and impingement effects on aquatic organisms. The recently proposed EPA regulations require that power plants currently using once-through cooling systems at the very minimum, evaluate the cost and environmental benefits of retrofitting to wet or dry cooling towers for their next permit application. However, a sound cooling tower retrofit assessment cannot be confined to cooling tower issues alone. Cooling tower backfits significantly affect the entire cooling system and generating capacity. Though the industry still awaits the EPA’s February 2004 final action ruling to clarify the regulations for existing plants, it is clear that acceptable methods of plant compliance with 316(b) regulations will be decided based upon the costs of new technology available, including cooling tower retrofits. A plant not able to meet the tight impingement and entrainment reduction percentages required under 316(b) will be required to consider the cost of retrofitting technologies versus the expected environmental benefit. The EPA has complied standard costs for retrofitting cooling towers that are extremely optimistic and limited in their scope, and thus tend to be far lower than a plant would actually accrue during a retrofit. These EPA costs of compliance are accepted by default in the cost-benefit analysis unless a plant can make a compelling case that their site-specific costs are much higher than EPA’s estimate or are wholly disproportionate to the environmental benefits accrued by such a retrofit. In either case, an overly simplistic and non-comprehensive tower retrofit cost estimate will increase the chances of a plant being required to implement a closed-cooling system retrofit, which in nearly all cases is the most costly and difficult alternative. In addition to constructing a tower, a cooling tower retrofit also alters many parts of the existing cooling system. Typically, a once-through condenser is designed to operate in a siphon circuit using low pressure buried piping under the turbine building. The condenser, along with its piping, would likely have to be modified to be compatible for a conversion to a higher pressure closed-loop system. The retrofit would require installation of new circulating water pumps to provide the additional required head. Portions of the plant’s large diameter circulating water piping systems and intakes must be decommissioned or redesigned to accommodate the retrofit. The critical parts of any retrofit evaluation will be to identify the site-specific modifications required for a conversion with a reasonably accurate estimate of capital costs. An accurate retrofit evaluation must reflect the impacts on all of the circulating water system components along with the adjusted overall performance. Obtaining accurate cost data on the full scope of a retrofit project is difficult due to many factors. There have been only a handful of cooling tower retrofits in the U.S. The experiences from these are mostly inapplicable due to either their small size or unique factors that facilitated the cooling system conversion. The site-specific nature of each retrofit, including the interpretation of a matrix of environmental siting issues, makes cooling system retrofit estimates very complex. Developing an accurate estimate requires a thorough review the existing cooling system design equipment, features & layout. These data are best obtained from a site visit and interviews with key system and operations personnel. Retrofit budgets for this evaluation should not be based on very “generic” cases prepared without regard to site-specific design & operating limitations. Instead, a realistic turnkey retrofit budget is based on a well planned project that confronts the broad scope of a retrofit including the range of site-specific factors. This paper will summarize the art of the retrofit and provide considerations to develop more reliable and meaningful closedcycle retrofit cooling system cost estimates. It will describe the critical characteristics of cooling towers, pumps, circulating water piping, and condenser modifications. It will provide recommendations to produce reasonably accurate evaluations of the seasonal and peak period (energy penalty) effects of the retrofitted cooling system on plant generation. In fact, those conversion costs and the negative effects on plant generation are the key to determining the realistic effects of a proposed retrofit. Finally, it will present the major consequences of trading-off the adverse aquatic environmental impacts with airborne ones from a retrofitted wet cooling tower.


2012 ◽  
Vol 232 ◽  
pp. 218-222
Author(s):  
Samad Ghafarigousheh ◽  
Ali Akbar Golneshan

In this paper a 3-D numerical model is used to investigate the thermal performance of a three aligned unit of NDDCT under crosswind condition. The computed results show that, there are major differences in computed velocity patterns and pressure fields around the cooling tower due to neighboring of a number of cooling towers will result considerable changes in computed flow parameters hence; the thermal performance losses for the single tower under crosswind are superior to those when this towers are incorporated in aligned arrangement. Results also show that the best thermal performance of the three aligned NDDCT is achieved when the crosswind is directed along the towers connection line.


Author(s):  
Mostafa H. Sharqawy ◽  
John H. Lienhard ◽  
Syed M. Zubair

Seawater cooling towers have been used since the 1970s in power generation and other industries, so as to reduce the consumption of freshwater. The salts in seawater are known to create a number of operational problems, including salt deposition, packing blockage, corrosion, and certain environmental impacts from salt drift and blowdown return. In addition, the salinity of seawater affects the thermophysical properties that govern the thermal performance of cooling towers, including vapor pressure, density, specific heat, viscosity, thermal conductivity, and surface tension. In this paper, the thermal performance of seawater cooling towers is investigated using a detailed model of a counterflow wet cooling tower. The model takes into consideration the coupled heat and mass transfer processes and does not make any of the conventional Merkel approximations. In addition, the model incorporates the most up-to-date seawater properties in the literature. The model governing equations are solved numerically, and its validity is checked against the available data in the literature. Based on the results of the model, a correction factor that characterizes the degradation of the cooling tower effectiveness as a function of seawater salinity and temperature approach is presented for performance evaluation purposes.


Author(s):  
David Werth ◽  
Matthew Havice

Pump intake structures are a necessary component of the cooling water systems for power plants, process and manufacturing facilities, flood control and water/wastewater applications. Large cooling water systems often use substantial sea / river water intakes or cooling towers to provide the required cooling of the process or circulating water. These structures can be very large and often house multiple pump with capacities ranging in size from a few hundred m3/hr to 60,000 m3/hr or more. With such large flow rates care must be taken to ensure uniform flow to the pump to limit vortex activity, vibration, flow induced cavitation and performance problems. In many cases, a physical hydraulic model study is conducted to evaluate the overall approach flow and the performance of the intake. This paper presents a synopsis of several recent physical model studies and a review of recurring problems associated with common design features. This paper takes a closer look at stop log support walls, an intake design feature common to seawater intakes. This wall is often used to minimize the height of the stop logs. In applications with large variations of water level, such as a seawater intake, there are times when the support walls are submerged significantly, resulting in significant flow disturbances. A feature common to cooling towers is the use of 90-degree suction elbows to supply horizontal pumps. A review of short radius vs. long radius elbow performance is presented. Cooling towers often have another common feature which is a significant difference in depth between the cooling tower basin and the pump sump. This results in typical shallow basins and deeper sumps. A common problem is the utilization of minimum pump submergence to set the water levels without reference to the basin invert elevation. A discussion of choked flow conditions in cooling towers is presented. A final discussion is presented regarding cross-flow and the use of concentrated supply channels in cooling tower applications to facilitate the isolation of individual tower cells. This paper presents a synopsis of several recent physical model studies and a review of recurring problems associated with common intake design features. The results of several model studies are presented to demonstrate the negative impacts that these common intake features have on approach flow conditions. The intent of the paper is to provide the design engineer some additional guidance not offered in industry guidelines or standards with the hope of avoiding common problems which can be costly and difficult to remediate after the intake has been constructed.


2014 ◽  
Vol 87 ◽  
pp. 530-538 ◽  
Author(s):  
Arash Mirabdolah Lavasani ◽  
Zahra Namdar Baboli ◽  
Mohsen Zamanizadeh ◽  
Masoud Zareh

1992 ◽  
Vol 114 (4) ◽  
pp. 632-642 ◽  
Author(s):  
B. R. Becker ◽  
L. F. Burdick

In the use of wet cooling towers, drift refers to small droplets of circulating water that are carried out of the cooling tower by the saturated exhaust air. Inertial impaction separators, known as drift eliminators, are used to strip the water droplets from the exhaust air. To achieve peak cooling tower operating efficiency, it is desirable that losses in fan system performance due to the drift eliminators be minimized. Therefore, an experimental program was developed and executed to evaluate the effect of drift eliminator design on cooling tower fan system performance. Flow visualization studies were used to gain insight into the flow patterns within the cooling tower plenum as influenced by drift eliminator design. A fully instrumented fan test cell was used to investigate the effects upon fan system performance resulting from two different styles of drift eliminators. The effect of drift eliminator discharge angle upon fan system total efficiency was investigated and the optimal discharge angle determined.


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