Retrofitting Cooling Towers: Estimates Required to Achieve the Next Level of CWA 316(b) Compliance

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.

1976 ◽  
Vol 98 (4) ◽  
pp. 450-456
Author(s):  
S. C. Yao ◽  
V. E. Schrock

The characteristics of inertial drift eliminators of wet cooling towers are studied parametrically for their blade shapes, orientation with respect to gravity, solidity ratios, blade sizes, approaching air speed, and drift spectrum. The fundamental behavior of drift eliminators is revealed by nondimensional parameters. A method for the optimum design of an eliminator considering minimum cost versus performance is developed. This methodology can be integrated into the optimum design of the whole cooling system. An example is shown for this design approach. Suggestions on the design to improve the drainage of the collected water are given.


2020 ◽  
Vol 2020 (2) ◽  
pp. 1-9
Author(s):  
Mykola Bosak ◽  
◽  
Oleksandr Hvozdetskyi ◽  
Bohdan Pitsyshyn ◽  
Serhii Vdovychuk ◽  
...  

Analytical hydraulic researches of the circulating water cooling system of the power unit of a thermal power plant with Heller cooling tower have been performed. Analytical studies were performed on the basis of experimental data obtained during the start-up tests of the circulating water cooling system of the “Hrazdan-5” power unit with a capacity of 300 MW. Studies of the circulating water cooling system were carried out at an electric power of the power unit of 200 - 299 MW, with a thermal load of 320 - 396 Gcal/hr. By circulating pumps (CP), water mixed with condensate is fed to the cooling tower, from where it is returned through the turbine for spraying by nozzles in the turbine steam condenser. An attempt to increase the water supply to the condenser by increasing the size of the nozzles did not give the expected results. The amount of the water supply to the circulating pumping station depends on the pressure loss in the circulating water cooling system. The highest pressure losses are in hydro turbines (HT), which are part of the circulating pumping station. Therefore, by adjusting the load of the hydro turbine, with a decrease in water pressure losses, you can increase the water supply by circulating pumps to the condenser. Experimental data and theoretical dependences were used to calculate the changed hydraulic characteristics of the circulating water cooling system. As a result of reducing the pressure losses in the section of the hydro turbine from 1.04 to 0.15 kgf/cm2, the dictating point for the pressure of circulating pumping station will be the turbine steam condenser. The thermal power plant cooling tower is designed to service two power units. Activation of the peak cooler sectors of the cooling tower gives a reduction of the cooled water temperature by 2-4 °С only with the spraying system.


2018 ◽  
Vol 29 (2) ◽  
pp. 245-259 ◽  
Author(s):  
Milica Jović ◽  
Mirjana Laković ◽  
Miloš Banjac

The electric power system of the Republic of Serbia relies mostly on lignite-fired thermal power plants, with 70% of the total electricity generation. Most of these plants are over 30 years old, and investment in their modernization is necessary. The energy efficiency of the 110 MW coal-fired power plant in which the condenser is cooled by the mechanical draught wet cooling towers system is analyzed in this paper. Attention is primarily devoted to operating conditions of the cold end of the plant, i.e. to the interrelationship of the condenser and cooling towers. Most important parameters that affect the operation of the cooling towers system are ambient air temperature and relative humidity, specific mass flow rate, and temperature of cooled water. With the existing cooling system, the overall energy efficiency of the plant is low, especially in the summer months, even less than 30%, due to adverse weather conditions. By upgrading existing cooling tower system by adaptation of two additional cooling tower cells, overall energy efficiency can be increased by 1.5%. The cooling tower system rehabilitation investments payback period is estimated to be less than one year. Static method for economic and financial assessment is used.


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):  
Hector L. Cruz

It has always been difficult to estimate size and cost of well designed counterflow induced-draught cooling towers due to the interrelationship of approach temperature and cooling range associated with each design. Attempts to estimate the cost of a tower by assessing currency per cell, per square foot, per gallon, or currency per other single metric, have never been sufficiently accurate due to the asymptotic nature of the approach temperature versus the tower size arithmetic function. To determine accurate qualitative metrics for cooling tower estimating purposes requires assessing two-variable second-order equations in water-flow-rate/approach-temperature, temperature-range/approach-temperature, wet-bulb-temperature/approach-temperature, and approach-temperature/cost. The design and therefore cost responds to the following variables; 1) Recirculating Water Flow Rate, 2) Inlet Wet Bulb Temperature (WBT), 3) Approach Temperature, and 4) Cooling Tower Range or Heat Duty. With the proper evaluation of these parameters they can be utilized to determine metrics to estimate the following parameters: 1) Number of Cells, 2) Basin Area, 3) Pump Power, 4) Fan Power, and 5) Costs (at today’s prices only). In addition, a percentage breakdown can be calculated for; 1) Structure, 2) Hardware, 3) Mechanical Equipment, 4) Labor, and 5) Miscellaneous items. Although developed for the power industry, the operative model, design, and qualified costing techniques are also valid for large petroleum and chemical process projects, provided the heat duty dissipated, ambient conditions, water quality and flow rate can be accurately predicted. A set of equations are developed which can be used to estimate the significant costs of a proposed cooling tower. Example calculations and data are presented in Annex A.


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.


2002 ◽  
Vol 2 ◽  
pp. 1-11
Author(s):  
Richard McLean ◽  
William A. Richkus ◽  
Stephen P. Schreiner ◽  
David Fluke

Maryland’s cooling-water intake and discharge regulations, the Code of Maryland Regulations (COMAR) 26.08.03, stem from Sections 316(a) and (b) of the Clean Water Act (CWA). COMAR 26.08.03.05 and litigative and administrative rulings stipulate that the location, design, construction, and capability of cooling-water intake structures must reflect the best technology available (BTA) for minimizing adverse environmental impacts (AEIs), providing that the costs of implementing the BTA are not wholly disproportionate to the expected environmental benefits. Maryland law exempts facilities that withdraw less than 10 million gallons/day (MGD) and less than 20% of stream or net flow by the intake. If not exempt, BTA must be installed if the cost of doing so is less than five times the value of fish impinged annually. Through site-specific studies and the use of a Spawning and Nursery Area of Consequence (SNAC) model applied to Representative Important Species, several power plants were evaluated to determine if they have had an adverse effect on spawning and nursery areas of consequence. Examples of application of the Maryland law to a number of power plants in the state are presented, together with the outcome of their evaluation.


Author(s):  
Shubham Rathi ◽  
S. S. Angalekar

Hyperbolic cooling towers have become the design standard for all natural-draft cooling towers because of their structural strength and minimum usage of material. The hyperbolic shape is particularly suited to cooling tower construction as the wide base provides a large space for the water and cooling system. As the tower widens out at the top, it supports the turbulent mixing as the heated air makes contact with the atmospheric air. Hyperbolic cooling tower is a tall structure with shells subjected to dead load and wind load. In absence of ground motion, wind becomes the major factor. In this study, 2 major models are studied with I and V column support. Each model is further divided into 2 models, i.e. one with SHELL element and another with SOLID element. All models were modelled and analyzed in ANSYS. The wind loads on these cooling tower have been calculated in the form of pressure by using the circumferentially distributed design wind pressure coefficients as given in IS: 11504 - 1985 code along with the design wind pressures at different levels as per IS: 875 (Part 3) - 1987 code. The analysis has been carried out using 8 noded shell element (SHELL281), 8 noded solid element (SOLID185) and 20 noded solid element (SOLID 186).


Energies ◽  
2019 ◽  
Vol 12 (2) ◽  
pp. 260 ◽  
Author(s):  
Adriana Estokova ◽  
Marcela Ondova ◽  
Martina Wolfova ◽  
Alena Paulikova ◽  
Stanislav Toth

A comprehensive understanding of the environmental impacts of buildings is not possible without knowledge of the technical and environmental properties of the materials that are used for their construction. This paper evaluates the environmental impacts of 156 material variations of conventional compositions of external bearing walls, which represent a significant part of a building’s envelope. Environmental (embodied energy, global warming potential, effects to human health, damage to ecosystems, and resources availability) and technical (surface temperature, number of layers, thickness, and weight) parameters are investigated for structures with similar heat transfer coefficients (U = 0.21–0.22 W/(m2·K)). Based on a multi-criteria analysis, an optimal material composition, consisting of aerated concrete with graphite polystyrene, was identified. By analyzing the costs of the best material compositions, it is observed that constructions with environmental benefits do not result in an increase in the cost of the construction. On the contrary, at present, they represent an approximately 10% cheaper solution.


2020 ◽  
pp. 637-656 ◽  
Author(s):  
Marco Medici ◽  
Søren Marcus Pedersen ◽  
Giacomo Carli ◽  
Maria Rita Tagliaventi

The purpose of this study is to analyse the environmental benefits of precision agriculture technology adoption obtained from the mitigation of negative environmental impacts of agricultural inputs in modern farming. Our literature review of the environmental benefits related to the adoption of precision agriculture solutions is aimed at raising farmers' and other stakeholders' awareness of the actual environmental impacts from this set of new technologies. Existing studies were categorised according to the environmental impacts of different agricultural activities: nitrogen application, lime application, pesticide application, manure application and herbicide application. Our findings highlighted the effects of the reduction of input application rates and the consequent impacts on climate, soil, water and biodiversity. Policy makers can benefit from the outcomes of this study developing an understanding of the environmental impact of precision agriculture in order to promote and support initiatives aimed at fostering sustainable agriculture.


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